Carbene transition metal catalysts

ABSTRACT

The present invention relates to novel complexes of (transition) metals containing ligands having phosphorus centers supporting a carbene structure or heteroalkane radical bonded to the (transition) metal.

CROSS-REFERENCE TO RELATED APPLICATIONS

This application is a continuation-in-part of U.S. Ser. No. 09/216,041, filed Dec. 18, 1998, now abandoned.

FIELD OF THE INVENTION

The present invention relates to novel catalysts of metals preferably transition metals and to the processes for using such catalysts for olefin polymerization. The catalyst contains at least one phosphorus center, and a carbon atom or an alkenyl radical bonded to the metal to form a metal heteroatom alkyl bond or a carbene structure, respectively.

BACKGROUND OF THE INVENTION

Currently there is increasing interest in catalysts of transition metals having novel structures.

Recently there has been significant interest in Brookhart's ligand which may complex later transition metals to form a catalyst useful in an olefin polymerization process. Such complexes are disclosed for example in World patent application 96/23010 jointly in the names of the University of Carolina at Chapel Hill and E.I. DuPont published Aug. 1, 1996. The Brookhart et al patent application does not teach the complexes of the present invention.

The recent paper (Chem. Comm (1998) p. 849) by Gibson and coworkers at Imperial College UK (and BP) teach complexes having a novel structure that is dissimilar to the complexes of the present invention. It is postulated that the complexes of Gibson et al will have utility in the polymerization of certain monomers such as alpha olefins.

There has been a great deal of work recently by both Exxon in the field of metallocene chemistry and by the Dow Chemical Company in single site constrained geometry complexes. As far as applicant has been able to determine none of the chemistry proposed by either Exxon or Dow contain a carbene structure or a constrained alkyl carbon bonded to a transition metal. There are several patents relating to amidinato complexes of transition metals which are suitable for the polymerization of various olefins. U.S. Pat. No. 5,502,128 issued Mar. 26, 1996, assigned to University of Massachusetts, teaches such complexes may be used to polymerize vinyl aromatic monomers; and U.S. Pat. No. 5,707,913 Issued Jan. 13, 1998, assigned to BASF, teaches such compounds may be used to polymerize olefins. Neither of these patents disclose complexes of the structure of the present invention.

U.S. Pat. No. 5,557,023 issued September, 1996 teaches the use of some complexes of transition metals to oligomerize lower alpha olefins such as ethylene to higher olefins such as hexene and the like. The complexes of the patent do not contain a carbene structure or substituted carbon bonded to the transition metal.

Copending U.S. patent application Ser. No. 09/174,782 filed Oct. 22, 1998 in the name of R. G. Cavell et al discloses the complexes useful in the catalyst of the present invention.

Applicant has been unable to identify any prior art disclosing the catalyst of the present invention for the polymerization of olefins.

SUMMARY OF THE INVENTION

The present invention provides a process for the polymerization of one or more C₂₋₁₂ alpha olefins in the presence of a complex selected from the group consisting of:

(a) a complex of formula I: ##STR1## wherein M is a metal atom; R¹, R², R³ and R⁴ are independently selected from the group consisting of a hydrogen atom, a saturated or unsaturated straight chained, branched or cyclic hydrocarbyl radical which is unsubstituted or substituted by one or more substituents selected from the group consisting of a halogen atom and a C₁₋₆, most preferably a C₁₋₄ alkyl radical; R⁷ and R⁸ are independently selected from the group consisting of a hydrogen atom, a halogen atom, an amide --NR¹ R², imide ═NR¹, alkoxide or aryl oxide group --OR¹, and an --OSi(R¹)₃ group where R¹ and R² are defined above, and a saturated or unsaturated straight chained, branched or cyclic hydrocarbyl radical which are unsubstituted or substituted by a halogen atom or a C₁₋₆ alkyl radical or a Lewis base (neutral coordinating ligands) which may contain a donor heteroatom including but not limited to ethers, tertiary amines, tertiary phosphines and cyclic amines; and each R⁵ is independently selected from the group consisting of radicals selected from the group consisting of saturated and unsaturated straight chained, branched and cyclic hydrocarbyl radicals, preferably C₁₋₁₅ saturated or unsaturated straight chained, branched or cyclic hydrocarbyl radicals most preferably C₁₋₈ straight or branched alkyl radicals and C₆₋₁₂ cyclic aliphatic or aromatic radical; radicals of the formula Si(R⁶)₃ wherein each R⁶ is independently selected from the group consisting of saturated or unsaturated straight chained, branched or cyclic hydrocarbyl radicals, preferably C₁₋₁₀ saturated or unsaturated straight chained, branched or cyclic hydrocarbyl radicals; and radicals of the formula III: ##STR2## wherein R⁹, R¹⁰, R¹¹ and R¹² are independently selected from the group consisting of a hydrogen atom, a fluorine atom, a NO₂ radical, a C₁₋₆ alkyl radical, and a C₈₋₁₂ aryl radical and E is an endocyclic nitrogen atom or a C--CN group;

(b) a complex of formula II: ##STR3## wherein M, R¹, R², R³, R⁴, R⁵, R⁷ and R⁸ are as defined above and R¹⁴ is selected from the group consisting of a hydrogen atom and a C₁₋₂₀ hydrocarbyl radical which may contain a terminal functional group; preferably a hydrogen atom or a C₁₋₄ alkyl radical. Optionally, R¹⁴ taken together with a transitional metal may form a constrained ring; and

c) a complex of formula V: ##STR4## wherein M, R¹, R², R³, R⁴ and R⁵ are as defined above, and an activator at a temperature from 20 to 250° C. and at a pressure from 15 to 15,000 psi.

The present invention also provides a complex of formula II: ##STR5## wherein M, R¹, R², R³, R⁴, R⁵, R⁷, R⁸ and R¹⁴ are as defined above.

The present invention further provides a complex of the formula V: ##STR6## wherein M, R¹, R², R³, R⁴ and R⁵ are as defined above, preferably each M is the same.

DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS

The term "scavenger" as used in this specification is meant to include those compounds effective for removing polar impurities from the reaction solvent. Such impurities can be inadvertently introduced with any of the polymerization reaction components, particularly with solvent, monomer and catalyst feed; and can adversely affect catalyst activity and stability. It can result in decreasing or even elimination of catalytic activity, particularly when an activator capable of ionizing the catalyst is also present.

In the catalyst of the present invention, the metal may be any transition metal. It may be an early transition metal such as Y, Ti, Zr, Hf, V or Cr or it may be a later transition metal such as Fe, Co, Ni, Pd or Pt or a post transition metal (Zn) or a lanthanide group, preferably Sm. Preferably the transition metal will be selected from group 3 through 10 (formerly group IIIB through VIII) of the periodic table.

In accordance with the present invention R¹, R², R³ and R⁴ may be independently selected from the group consisting of a hydrogen atom, a saturated or unsaturated straight chained, branched or cyclic hydrocarbyl radical which is unsubstituted or substituted by one or more substituents selected from the group consisting of a halogen atom and a C₁₋₆, most preferably a C₁₋₄ alkyl radical. Preferably, the hydrocarbyl radicals may be selected from the group consisting of a C₁₋₁₀, preferably C₁₋₈, most preferably C₁₋₆ straight chained, branched or cyclic alkyl radicals which radicals may be unsubstituted or further substituted, preferably by not more than three substituents selected from the group consisting of C₁₋₄ alkyl radicals or a halogen atom, preferably either F or Cl. Additionally, substituents R¹, R², R³ and R⁴ may be independently selected from the group consisting of C₅₋₁₄ aromatic radicals which radicals are unsubstituted or substituted by up to n-1, wherein n is the number of carbon atoms in the aromatic radical, substituents selected from the group consisting of a halogen atom, preferably F or Cl, a C₁₋₆, most preferably a C₁₋₄ alkyl radical or an amido radical which is unsubstituted or substituted by up to two C₁₋₆, preferably C₁₋₄ alkyl radicals.

The substituents R¹, R², R³ and R⁴ may be selected from the group consisting of a hydrogen atom, a fluorine atom, a chlorine atom, a methyl radical, an ethyl radical, a propyl radical, a butyl radical, a tertiary butyl radical and a phenyl radical.

In some embodiments of the present invention R¹ and R² may be the same. In a further embodiment R³ and R⁴ may be the same. In a further embodiment of the present invention all of R¹, R², R³ and R⁴ may be the same.

In the present invention R⁷ and R⁸ may be independently selected from the group consisting of a halogen atom, an amide --NR¹ R², an alkoxide or aryl oxide group --OR¹, and an --OSi(R¹)₃ group wherein R¹ and R² are defined above; and a saturated or unsaturated straight chained, branched or cyclic hydrocarbyl radical which are unsubstituted or substituted by a halogen atom or a C₁₋₆ alkyl radical. The hydrocarbyl radical may be a straight chained or branched C₁₋₁₀ alkyl radical which may be unsubstituted or substituted by a F or Cl atom or up to three C₁₋₆, preferably C₁₋₄ alkyl radicals. The hydrocarbyl radical may be selected from the group consisting of C₅₋₁₄ aromatic radicals which radicals are unsubstituted or substituted by up to n-1, wherein n is the number of carbon atoms in the aromatic radical, substituents selected from the group consisting of a halogen atom, preferably F or Cl, a C₁₋₆, most preferably a C₁₋₄ alkyl radical or an amido radical which is unsubstituted or substituted by up to two C₁₋₆, preferably C₁₋₄ alkyl radicals. In one embodiment of the invention at least one of R⁷ and R⁸ may be C₅₋₁₃ ligand containing a 5-membered carbon ring having delocalized bonding within the ring and typically being bound to the metal through covalent η⁵ --bonds such as cyclopentadienyl, indenyl or fluorenyl ligands which are unsubstituted or up to fully substituted by a halogen atom, preferably chlorine or fluorine, a C₁₋₄ alkyl radical or an amido radical which is unsubstituted or substituted by up to two C₁₋₄ alkyl radicals.

In accordance with the present invention each R⁵ is independently selected from the group consisting of radicals of a saturated or unsaturated straight chained, branched or cyclic hydrocarbyl radical, preferably C₁₋₁₅ saturated or unsaturated straight chained, branched or cyclic hydrocarbyl radicals, most preferably a C₁₋₈ straight or branched alkyl radical and a C₆₋₁₂ cyclic aliphatic or aromatic radical; radicals of the formula Si(R⁶)₃ wherein each R⁶ is independently selected from the group consisting of saturated or unsaturated straight chained, branched or cyclic hydrocarbyl radicals, preferably C₁₋₁₀ saturated or unsaturated straight chained, branched or cyclic hydrocarbyl radicals preferably C₁₋₁₀ saturated or unsaturated straight chained, branched or cyclic hydrocarbyl radicals; radicals of the formula III: ##STR7## wherein R⁹, R¹⁰, R¹¹ and R¹² are independently selected from the group consisting of a hydrogen atom, a fluorine atom, a NO₂ radical, a C₁₋₆ alkyl radical, and a C₈₋₁₂ aryl radical and E is an endocyclic nitrogen atom or a C--CN group.

Each R⁵ radical may be selected from the group consisting of radicals of the formula Si(R⁶)₃ wherein each R⁶ is independently selected from the group consisting of saturated or unsaturated straight chained, branched or cyclic hydrocarbyl radicals, preferably C₁₋₁₀ saturated or unsaturated straight chained, branched or cyclic hydrocarbyl radicals. Most preferably R⁶ is selected from C₁₋₈, preferably C₁₋₆, most preferably C₁₋₄ alkyl radicals. Suitable alkyl radicals include methyl, ethyl, propyl and butyl radicals. In a preferred embodiment of this aspect of the invention each R⁶ radical is the same.

Each R⁵ radical may be selected from the group consisting of radicals of the formula III: ##STR8## wherein R⁹, R¹⁰, R¹¹ and R¹² are independently selected from the group consisting of a hydrogen atom, a fluorine atom, a NO₂ radical, a C₁₋₆ alkyl radical, and a C₈₋₁₂ aryl radical and E is an endocyclic nitrogen atom or a C--CN group. Such radicals include the 4-cyanotetrafluorophenyl radical.

Independently each R⁵ radical may be selected from the group consisting of saturated or unsaturated straight chained, branched or cyclic hydrocarbyl radicals, preferably C₁₋₁₅ saturated or unsaturated straight chained, branched or cyclic hydrocarbyl radicals most preferably a C₁₋₈ straight or branched alkyl radical and a C₆₋₁₂ cyclic aliphatic or aromatic radical. Some hydrocarbyl radicals include methyl, ethyl, butyl, phenyl and adamantyl radicals.

The complexes of formula I of the present invention may be prepared by reacting a compound of the formula VI: ##STR9## wherein R¹, R², R³, R⁴ and R⁵ are as defined above with a compound of the formula M(X)_(s) (Y)_(t) (L)_(n) wherein M is as defined above, X is independently selected from a group consisting of an alkyl, preferably having from 1 to 10 carbon atoms which is unsubstituted or substituted by a C₁₋₄ alkyl radical or a C₆₋₁₀ aryl (e.g. benzyl) radical, a silylated amido or imido complex --N(SiR⁵ ₃)₂ or ═N(SiR⁵ ₃) wherein R⁵ is defined above, or imido ═NR radicals where R is a C₁₋₁₀ alkyl or a C₆₋₁₀ aryl radical, Y is a halogen atom, an alkoxy radical and an alkyl or amide radical preferably having from 1 to 10 carbon atoms and aryloxy radical preferably having from 6 to 10 carbon atoms, and the sum of s and t equal the valence of the transition metal M and provided that at least two of the X and Y groups can be eliminated from the molecule, in a C₅₋₁₂ hydrocarbyl solvent or a C₂₋₁₀ ether solvent at a temperature from 20 to 150° C. Suitably X and Y radicals include but are not limited to bis(trimethylsilyl) amido; benzyl; and suitable Lewis bases include, but are not restricted to diethyl ether or tetrahydrofuran. L is a Lewis base (neutral coordinating ligands) which may contain a donor heteroatom including but not limited to ethers, tertiary amines, tertiary phosphines and cyclic amines. Some suitable Lewis bases (neutral coordinating ligands) comprise one or more donor heteroatoms including but not limited to C₁₋₆ alkyl ethers, C₄₋₈ cyclic ethers, C₁₋₆ tertiary amines, cyclic nitrogen aromatics from 4 to 8 carbon atoms such as pyridine, or tertiary C₁₋₁₀ phosphines, and n may range from 0 to 3. The final form of the compound may retain some of the Lewis bases components defined as L or a similar species obtained from the reaction solvent. Alternatively the compound above of the formula VI may be reacted with two moles of alkyl lithium reagent to prepare the dilithio derivative of the formula IV {R¹ R² {N(R⁵)}PC(Li)₂ PR³ R⁴ {N(R⁵)}: ##STR10## which in turn can be reacted with metal halide or alkyl halide precursors M(X)_(s) (Y)_(t) (L)_(n) as defined above containing at least two halogen atoms as replaceable substituents in the X and Y group.

The catalyst of the present invention wherein the R⁷ and R⁸ are halogens and may be alkylated, aminated or alkoxylated by reacting with suitable alkylating agents such as LiR or RMgX, aminating agents such as MNR₂ or an alkoxylating agent which is an alkali alkoxide (e.g. M² OR where M² is selected from the group consisting of alkali metals, preferably lithium). In the alkylating, aminating or alkoxylating agent, the alkyl or alkoxide radical is as defined in R⁷ and R⁸ above.

Some hydrocarbon solvents include C₅₋₁₂ hydrocarbons which may be unsubstituted or substituted by C₁₋₄ alkyl group, such as pentane, hexane, heptane, octane, cyclohexane, methylcyclohexane and hydrogenated naphtha. An additional solvent is Isopar E (C₈₋₁₀ aliphatic solvent, Exxon Chemical Co.). The solvent may be aromatic such as benzene, toluene or xylene. The solvent may also be a simple or branched ether in which the alkyl radicals may contain from 1 to 10 carbon atoms or a polyether thereof such as diethyl ether and diglyme. The product is recovered using conventional procedures illustrated in the examples. The reaction may be carried out from room temperature (20° C.) to about 150° C.

In the compounds of formula II, M, R¹, R², R³, R⁴, R⁵, R⁷ and R⁸ are as defined above and R¹⁴ is selected from the group consisting of a hydrogen atom and a C₁₋₂₀ hydrocarbyl radical which may contain a terminal functional group such as an amido group which may be unsubstituted or substituted by a C₁₋₄ alkyl radical; preferably a hydrogen atom or a C₁₋₄ alkyl radical. In an optional but desirable embodiment R¹⁴ taken together with a transitional metal may form a constrained ring.

The compounds of formula II may be prepared by addition of an unsaturated molecular system to the M═C bond in a compound of formula I or by the addition of a molecule AB (where A and B may be hydrogen, an alkyl or aryl group, or substituted groups of the type RO, RS, RR'N, RR'P and the like). The products may or may not have a cyclic structure.

The catalyst of the present invention wherein R⁷ and R⁸ are not alkyl may be alkylated (either partially or fully). Some alkylating agents are Grignard agents of the formula RMgX and organolithium reagents of the formula LiR wherein R is a C₁₋₁₀ alkyl radical and X is a halogen and alkyl aluminum reagents. Alkyl aluminum reagents include trialkyl aluminum, alkyl aluminum halides (i.e. (R)_(x) AlX_(3-x), wherein R is a C₁₋₁₀ alkyl radical, X is a halogen, x is 1 or 2 and MAO as described below).

The polymerization may be conducted at temperatures from about 20 to about 250° C. Depending on the product being made, this temperature may be relatively low such as from 20 to about 120° C. (preferably less than 120° C., i.e. 119° C. and below). The pressure of the reaction may be as high as about 15,000 psig for the older high pressure processes or may range from about 15 to 4,500 psig. The temperatures for solution processes tend to be higher, typically from 120 to 250° C.

Solution polymerization processes are fairly well known in the art. These processes are conducted in the presence of an inert hydrocarbon solvent typically a C₅₋₁₂ hydrocarbon which may be unsubstituted or substituted by C₁₋₄ alkyl group such as pentane, hexane, heptane, octane, cyclohexane, methylcyclohexane or hydrogenated naphtha. An additional solvent is Isopar E (C₈₋₁₂ aliphatic solvent, Exxon Chemical Co.).

Suitable olefin monomers may be ethylene and C₃₋₂₀ mono- and di-olefins. Preferred monomers include ethylene and C₃₋₁₂ alpha olefins which are unsubstituted or substituted by up to two C₁₋₆ alkyl radicals. Illustrative non-limiting examples of such alpha-olefins are one or more of propylene, 1-butene, 1-pentene, 1-hexene, 1-octene and 1-decene.

The polyethylene polymers which may be prepared in accordance with the present invention typically comprise not less than 60, preferably not less than 70, most preferably not less than 80 weight % of ethylene and the balance of one or more C₄₋₁₀ alpha olefins, preferably selected from the group consisting of 1-butene, 1-hexene and 1-octene.

The complexes of the present invention may require the use of a support. An exemplary list of support materials include metal oxides (such as silica, alumina, silica-alumina, titania and zirconia); metal chlorides (such as magnesium chloride); talc, polymers (including polyolefins); partially prepolymerized mixtures of a group 4 metal complex, activator and polymer; spray dried mixtures of the group 4 metal complex, activator and fine "inert" particles (as disclosed, for example, in European Patent Office Application 668,295 (to Union Carbide)).

The preferred support material is silica. In a particularly preferred embodiment, the silica has been treated with an alumoxane (especially methylalumoxane or "MAO") prior to the deposition of the group 4 metal complex. The procedure for preparing "supported MAO" which is described in U.S. Pat. No. 5,534,474 (to Witco) is preferred for reasons of economy. It will be recognized by those skilled in the art that silica may be characterized by such parameters as particle size, pore volume and residual silanol concentration. The pore size and silanol concentration may be altered by heat treatment or calcining. The residual silanol groups provide a potential reaction site between the alumoxane and the silica (and, indeed, some off gassing is observed when alumoxane is reacted with silica having residual silanol groups). This reaction may help to "anchor" the alumoxane to the silica (which, in turn, may help to reduce reactor fouling).

The preferred particle size, preferred pore volume and preferred residual silanol concentration may be influenced by reactor conditions. Typical silicas are dry powders having a particle size of from 1 to 200 microns (with an average particle size of from 30 to 100 being especially suitable); pore size of from 50 to 500 Angstroms; and pore volumes of from 0.5 to 5.0 cubic centimeters per gram. As a general guideline, the use of commercially available silicas, such as those sold by W. R. Grace under the trademarks Davison 948 or Davison 955, are suitable.

The activator may be selected from the group consisting of:

(i) an aluminoxane; and

(ii) an activator capable of ionizing the catalyst (which may be used in combination with an alkylating activator).

The aluminoxane activator may be of the formula (R²⁰)₂ AlO(R²⁰ AlO)_(m) Al(R²⁰)₂ wherein each R²⁰ is independently selected from the group consisting of C₁₋₂₀ hydrocarbyl radicals, m is from 0 to 50, and preferably R²⁰ is a C₁₋₄ alkyl radical and m is from 5 to 30. The aluminoxane activator may be used prior to the reaction but preferably in situ alkylation is typical (e.g. alkyl groups replacing leaving ligands, hydrogen or halide groups).

Activation with aluminoxane generally requires a molar ratio of aluminum in the activator to the catalyst from 20:1 to 1000:1. MAO may be the higher end of the above noted range.

The activator of the present invention may be a combination of an alkylating activator which also serves as a scavenger other than aluminoxane in combination with an activator capable of ionizing the catalyst.

The alkylating activator (which may also serve as a scavenger) may be selected from the group consisting of: (R)_(p) MgX_(2-p) wherein X is a halide, each R is independently selected from the group consisting of C₁₋₁₀ alkyl radicals, preferably C₁₋₈ alkyl radicals and p is 1 or 2; RLi wherein R is as defined above; (R)_(q) ZnX_(2-q) wherein R is as defined above, X is halogen and q is 1 or 2; (R)_(s) AlX₃₋ wherein R is as defined above, X is halogen and s is an integer from 1 to 3. Preferably, in the above compounds R is a C₁₋₄ alkyl radical and X is chlorine. Commercially available compounds include triethyl aluminum (TEAL), diethyl aluminum chloride (DEAC), dibutyl magnesium ((Bu)₂ Mg) and butyl ethyl magnesium (BuEtMg or BuMgEt).

The activator capable of ionizing the catalyst may be selected from the group consisting of:

(i) compounds of the formula [R¹⁵ ]⁺ [B(R¹⁸)₄ ]⁻ wherein B is a boron atom, R¹⁵ is a cyclic C₅₋₇ aromatic cation or a triphenyl methyl cation and each R¹⁸ is independently selected from the group consisting of phenyl radicals which are unsubstituted or substituted with from 3 to 5 substituents selected from the group consisting of a fluorine atom, a C₁₋₄ alkyl or alkoxy radical which is unsubstituted or substituted by a fluorine atom, and a silyl radical of the formula --Si-(R¹⁹)₃ wherein each R¹⁹ is independently selected from the group consisting of a hydrogen atom and a C₁₋₄ alkyl radical; and

(ii) compounds of the formula [(R¹⁶)_(t) ZH]⁺ [B(R¹⁸)₄ ]⁻ wherein B is a boron atom, H is a hydrogen atom, Z is a nitrogen atom or phosphorus atom, t is 2 or 3 and R¹⁶ is selected from the group consisting of C₁₋₈ alkyl radicals, a phenyl radical which is unsubstituted or substituted by up to three C₁₋₄ alkyl radicals, or one R¹⁶ taken together with the nitrogen atom to form an anilinium radical and R¹⁸ is as defined above; and

(iii) compounds (activators) of the formula B(R¹⁸)₃ wherein R¹⁸ is as defined above.

In the above compounds, preferably R¹⁸ is a pentafluorophenyl radical, R¹⁵ is a triphenylmethyl cation, Z is a nitrogen atom and R¹⁶ is a C₁₋₄ alkyl radical or R¹⁶ taken together with the nitrogen atom to form an anilinium radical which is substituted by two C₁₋₄ alkyl radicals.

The activator capable of ionizing the catalyst abstracts one or more of R⁷ or R⁸ so as to ionize the catalyst center into a cation, but not to covalently bond with the catalyst; and to provide sufficient distance between the ionized catalyst and the ionizing activator to permit a polymerizable olefin to enter the resulting active site.

Examples of compounds capable of ionizing the catalyst include the following compounds:

triethylammonium tetra(phenyl)boron,

tripropylammonium tetra(phenyl)boron,

tri(n-butyl)ammonium tetra(phenyl)boron,

trimethylammonium tetra(p-tolyl)boron,

trimethylammonium tetra(o-tolyl)boron,

tributylammonium tetra(pentafluorophenyl)boron,

tributylammonium tetra(pentafluorophenyl)boron,

tri(n-butyl)ammonium tetra(o-tolyl)boron,

N,N-dimethylanilinium tetra(phenyl)boron,

N,N-diethylanilinium tetra(phenyl)boron,

N,N-diethylanilinium tri(phenyl)n-butylboron,

N,N-2,4,6-pentamethylanilinium tetra(phenyl)boron,

di-(isopropyl)ammonium tetra(pentafluorophenyl)boron,

dicyclohexylammonium tetra(phenyl)boron,

triphenylphosphonium tetra(phenyl)boron,

tri(methylphenyl)phosphonium tetra(phenyl)boron,

tri(dimethylphenyl)phosphonium tetra(phenyl)boron,

tropillium tetrakispentafluorophenyl borate,

triphenylmethylium tetrakispentafluorophenyl borate,

benzene (diazonium) tetrakispentafluorophenyl borate,

tropillium phenyltrispentafluorophenyl borate,

triphenylmethylium phenyltrispentafluorophenyl borate,

benzene (diazonium) phenyltrispentafluorophenyl borate,

tropillium tetrakis (2,3,5,6-tetrafluorophenyl) borate,

triphenylmethylium tetrakis (2,3,5,6-tetrafluorophenyl) borate,

benzene (diazonium) tetrakis (3,4,5-trifluorophenyl) borate,

tropillium tetrakis (3,4,5-trifluorophenyl) borate,

benzene (diazonium) tetrakis (3,4,5-trifluorophenyl) borate,

tropillinum tetrakis (1,2,2-trifluoroethenyl) borate,

triphenylmethylium tetrakis (1,2,2-trifluoroethenyl) borate,

benzene (diazonium) tetrakis (1,2,2-trifluoroethenyl) borate,

tropillium tetrakis (2,3,4,5-tetrafluorophenyl) borate,

triphenylmethylium tetrakis (2,3,4,5-tetrafluorophenyl) borate, and

benzene (diazonium) tetrakis (2,3,4,5-tetrafluorophenyl) borate.

Readily commercially available activators which are capable of ionizing the catalyst include:

N,N-dimethylaniliniumtetrakispentafluorophenyl borate,

triphenylmethylium tetrakispentafluorophenyl borate, and

trispentafluorophenyl boron.

If the catalyst is activated with a combination of an aluminum alkyl compound (generally other than aluminoxane), and a compound capable of ionizing the catalyst; the molar ratios of catalyst:metal in the alkylating agent (e.g. Al): metalloid (e.g. boron or phosphorus) in the activator capable of ionizing the catalyst (e.g. boron) may range from 1:1:1 to 1:100:5. Preferably, the alkylating activator is premixed/reacted with the catalyst and the resulting alkylated species is then reacted with the activator capable of ionizing the catalyst.

In a solution polymerization, the monomers are dissolved/dispersed in the solvent either prior to being fed to the reactor or for gaseous monomers, the monomer may be fed to the reactor so that it will dissolve in the reaction mixture. Prior to mixing, the solvent and monomers are generally purified to remove polar moieties. The polar moieties or catalyst poisons include water, oxygen, metal impurities, etc. Preferably steps are taken before provision of such into the reaction vessel, for example by chemical treatment or careful separation techniques after or during the synthesis or preparation of the various components. The feedstock purification prior to introduction into the reaction solvent follows standard practices in the art (e.g. molecular sieves, alumina beds and oxygen removal catalysts) are used for the purification of ethylene, alpha-olefin and optional diene. The solvent itself as well (e.g. cyclohexane and toluene) is similarly treated. In some instances, out of an abundance of caution, excess scavenging activators may be used in the polymerization process.

The feedstock may be heated prior to feeding into the reactor. However, in many instances it is desired to remove heat from the reactor so the feedstock may be at ambient temperature to help cool the reactor.

Generally, the components may be premixed in the solvent for the reaction or fed as separate streams to the reactor. In some instances, premixing is desirable to provide a reaction time for the catalyst components prior to entering the reaction. Such an "in line mixing" technique is described in a number of patents in the name of DuPont Canada Inc. For example it is described in U.S. Pat. No. 5,589,555 issued Dec. 31, 1996.

The reactor may comprise a tube or serpentine reactor used in the "high pressure" polymerizations or it may comprise one or more reactors or autoclaves. It is well known that the use in series of two such reactors each of which may be operated so as to achieve different polymer molecular weight characteristics. The residence time in the reactor system will depend on the design and the capacity of the reactor. Generally, the reactors should be operated under conditions to achieve a thorough mixing of the reactants. On leaving the reactor system, the solvent is removed and the resulting polymer is finished in a conventional manner.

The present invention will be illustrated by the following non-limiting examples in which, unless otherwise specified, part means parts by weight (e.g. grams) and per cent means weight per cent.

Synthesis of Ligands and Metal Carbene Complexes

General Experimental Conditions for Catalyst Synthesis

All experimental manipulations were performed under rigorously anaerobic conditions using Schlenk techniques or an argon-filled glovebox with an efficient recirculator. Solvents were dried and distilled under argon prior to use. Hexane and toluene were distilled from Na-K and Na respectively. NMR solvents benzene-d₆ and toluene-d₈ were freshly vacuum transferred from Na-K. Commercial (Aldrich) supplies of dppm, Me₃ SiN₃, ZrCl₄ and HfCl₄ were used as obtained. NMR spectra were recorded using Bruker® WH-200, 300 and 400 spectrometers with reference to the deuterium signal of the solvent employed. The ¹ H NMR chemical shifts are reported in ppm from external Me₄ Si and the ³¹ P NMR spectra are reported in ppm from external 85% H₃ PO₄. Positive values reflect shifts downfield. Infrared spectra were recorded on a Nicolet® 7199 infrared spectrometer.

Preparation of Ligands

Preparation of CH₂ [Cy₂ P═NSiMe₃ ]₂

To a solution of dcpm, {Cy₂ P}₂ CH₂, (literature preparation: Fryzuk, M. D.; McConville, D. H.; Rettig, S. J.; J. Organomet. Chem. 1993, 445, 245-256.} (3.97 g, 9.72 mmol) in 60 mL of toluene was added trimethylsilyl azide (6 mL, 45.79 mmol) with stirring. The solution was heated to reflux at 110° C. for 48 hours. Solvent was evaporated under vacuum to obtain microcrystalline solid which was washed twice with hexane and dried (Yield: 4.85 g, 85.6%). IR (Nujol mull): 2666 w, 2653 w, 1449 s, 1376 m, 1348 m, 1302 s, 1264 s, 1244 s, 1233 s, 1209 m, 1173 m, 1154 m, 1119 w, 1078 w, 1045 w, 1028 w, 1004 m, 913 w, 896 m, 852 s, 827 s, 787 s, 776 s, 751 s, 675 m, 663 m, 633 m, 571 w, 526 m. ¹ H NMR (C₆ D₆): δ 1.95 (b. t, 4 H, CH-Cy methine), 1.7 (m, CH₂ -Cy methylene), 1.62 (d, ² J_(PH) =12.2 Hz, 2 H, PCH₂ P methylene), 1.40-1.05 (m, CH₂ -Cy methylene), 0.38 (s, 18 H, CH₃ Si methyl). ¹³ {¹ H} NMR (C₆ D₆): δ 39.5 (m, 4 C, CH-Cy methine), 27.1 (s, 4 C, para Cy), 27.0 (s, 8 C, ortho Cy), 26.8 (s, 4 C, meta Cy), 26.5 (s, 4 C, meta Cy), 21.6 (t, ¹ J_(PC) =61.6 Hz, 1 C, P CH₂ P methylene), 5.3 (s, 6 C, CH₃ Si). ¹³ C {¹ H, ³¹ P} (C₆ D₆): δ 39.5 (s, 4 C, CH-Cy, methine), 27.1 (s, 4 C, para Cy), 27.0 (s, 8 C, ortho Cy), 26.8 (s, 4 C, meta Cy), 26.5 (s, 4 C, meta Cy), 21.6 (s, 1 C, P CH₂ P methylene), 5.3 (s, 6 C, CH₃ Si). ³¹ P{¹ H} NMR (C₆ D₆): δ 14.6 (2 P). Analysis calculated for C₃₁ H₆₄ N₂ P₂ Si₂ : C, 63.87; H, 11.06; N, 4.81. Found: C, 63.55; H, 11.22; N, 4.63.

Preparation of CH₂ [Ph₂ P═NSiMe₃ ]₂

As described in the literature {Appel, R.; Ruppert, I. Z.; Anorg. Allg. Chem. 1974, 406, 131-144.}.

Preparation of CH₂ (Ph₂ P═NAd)₂

Adamantyl azide (1.66 g, 9.37 mmol) was added to a solution of bis(diphenylphosphino)methane (dppm) (1.80 g, 4.68 mmol) in 60 mL of toluene. The mixture was heated to reflux at 110° C. for 2 days. The solution was then cooled to room temperature, concentrated to about 20 mL and maintained at -15° C. to yield, after about 12 hours, a microcrystalline solid which was filtered and dried (Yield: 2.56 g, 80%). ¹ H NMR (toluene-d₈): δ 7.87 (b. s, 8 H, ortho-Ph), 7.05 (b. s, 12 H, meta and para-Ph), 3.48 (b. t, 2 H, CH₂), 1.99 (b.s, 3 H, CH-Ad), 1.93 (b. s, 6 H, CH₂ -Ad), 1.59 (b. s, 6 H, CH₂ -Ad). ³¹ P{¹ H} NMR (toluene-d₈): δ-15.4 (s). Analysis calculated for C₄₅ H₅₂ N₂ P₂ : C, 79.15; H, 7.68; N, 4.10. Found: C, 78.58; H, 7.93; N, 4.03.

Preparation of Me₃ Si═NPPh₂ CH₂ Ph₂ P═NC₆ F₄ -p-CN

To a solution of bis(diphenylphosphoranotrimethylsilylimino)methane (11.17 g, 20 mmol) in dichloromethane a solution of pentafluorobenzonitrile (4.05 g, 21 mmol) in dichloromethane (35 mL) was added at room temperature. Immediately the solution turned yellow and after stirring for 12 hours became orange. The solvent was completely removed in vacuo leaving the slightly orange colored crude product which was recrystallized from acetonitrile giving the pure ligand (yield 10.28 g, 78%; white cubic crystals; mp 198-200° C.). Analysis calculated for C₃₅ H₃₁ F₄ N₃ P₂ Si: C, 63.77; H, 4.69; N, 6.36. Found: C, 63.01; H, 4.70; N, 6.46. MS (EI, m/z): 659 (M⁺). ¹ H NMR (CD₂ Cl₂): phenyl rings δ 7.80 to 7.74 ppm, 7.57 to 7.29 ppm (m, 20H); PCH₂ P methylene, δ 3.75 ppm (`t`, 2H, ² J_(HP) 13.39 Hz); Me₃ Si methyl δ-0.29 ppm (s, 9H). ¹⁹ F{¹ H} NMR (CDCl₂): ortho δ -140.17 ppm (m, 2F); meta δ-153.32 ppm (m, 2F). ²⁹ Si{¹ H} NMR (CDCl₂), δ-10.59 ppm (d, ² J_(SiP) 20.49 Hz).

Preparation of {Li₂ C{Ph₂ P═NSiMe₃ }₂ }

Colorless crystalline bis (diphenylphosphoranotrimethysilylimino)methane H₂ C{Ph₂ P═NSiMe₃ }₂ (1.0 g, 1.79 mmol) was dissolved in 20 ml of toluene. To this toluene solution, PhLi (0.30 g, 3.59 mmol) was added with stirring. The reaction mixture was stirred at room temperature for 3 days. Approximately 100 mg of colorless solid was removed by filtration. The clear solution was reduced to one-half volume and allowed to stand at room temperature for 48 hours whereupon colorless crystals deposited. (Yield: 0.62 g, 60.7%). IR (Nujol mull): 1434 m, 1244 s, 1190 s, 1174 m, 1101 s, 1067 s, 852 s, 832 s, 764 m, 747 m, 725 m, 709 m, 696 s, 675 w, 663 w, 646 s, 618 w, 606 w, 539 s, 512 m. ¹ H NMR (C₆ D₆): δ 7.53-7.49 (m, phenyl), 7.04-6.93 (m, phenyl), 0.04 (s, CH₃ Si methyl). ¹³ C{¹ H} NMR (C₆ D₆): δ 139.0 (m, 4 C, ipso phenyl), 131.0 (t, ² J_(PC) =4.5 Hz, 8 C, ortho phenyl), 129.0 (s, 4 C, para phenyl), 127.8 (s, 8 C, meta phenyl), 4.4 (s, 6 C, CH₃ Si). ³¹ P{¹ H } NMR (C₆ D₆): δ 13.7 (2 P). Analysis calculated for C₃₁ H₃₈ Li₂ N₂ P₂ Si₂ : C, 65.25; H, 6.71; N, 4.91. Found: C, 65.27; H, 6.69; N, 4.60.

Preparation of Metal Carbene and Related Derivatives

Preparation of [ZrCl₂ {C(Cy₂ ═NSiMe₃)₂ }](Zr-3C)

[ZrCl₂ {N(SiMe₃)₂ }₂ ] (0.5 g, 1.04 mmol) {literature preparation: Andersen, R. A.; Inorg. Chem. 1979, 18, 1724-1725} was dissolved in 15 mL of toluene by stirring. Solid bisimine ligand, CH₂ (Cy₂ P═NSiMe₃)₂ (0.604 g, 1.04 mmol) was added to the solution which was then heated to reflux at 130° C. for five days. The pale yellow solution was concentrated to about 10 mL and left at room temperature for 24 hours whereupon pale yellow crystals formed which were isolated by filtration (0.42 g). The mother liquor was concentrated to 5 mL, hexane was added and the total mixture was cooled to -15° C. for 24 hours which yielded a second crop of product (0.15 g). Yield: 0.57 g, 75.2%). IR (Nujol mull): 1447 s, 1403 w, 1377 m, 1356 w, 1321 s, 1258 s, 1246 s, 1200 w, 1192 m, 1176 m, 1167 w, 1111 m, 1049 b.s, 998 m, 915 w, 887 m, 837 s, 779 m, 769 s, 753 m, 746 s, 679 m, 651 s, 634 m, 609 s, 551 s, 509 w, 495 m, 484 w, 465 w. ¹ H NMR (C₆ D₆): δ 2.1-1.1 (b. m, 40 H, CH₂ -Cy methylene), 1.76 (m, 4 H, CH-Cy methine) (as assigned from a ¹ H-¹³ C HMQC expt.), 0.51 (s, 18 H, CH₃ Si methyl). ¹³ C {¹ H} NMR (C₆ D₆): δ 86.9 (t, ¹ J_(PC) =156.0 Hz, 1 C, PCP carbene), 40.3 (m, 4 C, CH-Cy, methine), 26.8 (m, 8 C, ortho Cy), 26.6 (s, 4 C, para Cy), 26.3 (s, 4 C, meta Cy), 26.1 (s, 4 C, meta Cy), 3.4 (s, 6 C, CH₃ Si). ¹³ C {¹ H, ³¹ P} NMR (C₆ D₆): δ 86.9 (s, 1 C, PCP carbene), 40.3 (s, 4 C, CH-Cy, methine), 26.9 (s, 4 C, ortho Cy), 26.8 (s, 4 C, ortho Cy), 26.6 (s, 4 C, para Cy), 26.3 (s, 4 C, meta Cy), 26.1 (s, 4 C, meta Cy), 3.4 (s, 6 C, CH₃ Si). ³¹ P{¹ H} NMR (C₆ D₆): δ 35.5 (2 P). Analysis calculated for C₃₁ H₆₂ Cl₂ N₂ P₂ Si₂ Zr: C, 50.11; H, 8.41; N, 3.77. Found: C, 49.97; H, 8.68; 3.63.

Preparation of [ZrMe₂ {C(Cy₂ ═NSiMe₃)₂ }]Zr-3C(Me₂)

To a toluene solution (˜20 mL) of Zr-3C (0.207 g, 0.278 mmol) at -78° C. was added a 3M diethyl ether solution of MeMgBr (0.241 mL, 0.723 mmol). The reaction mixture was warmed to room temperature, stirred for 2 hours and pumped to dryness. The solid was extracted with heptane (3×15 mL) and the heptane extract was slowly evaporated to dryness. Colorless crystals of Zr-3C(Me₂) were obtained (136 mg, plus ˜30 mg left in flask).

Preparation of [ZrCl₂ {C(Ph₂ P═NSiMe₃)₂ }](Zr-3D)

[ZrCl₂ {N(SiMe₃)₂ }₂ ] {literature preparation: Andersen, R. A.; Inorg. Chem. 1979, 18, 1724-1725. } (1.0 g, 2.07 mmol) was dissolved in 20 mL of toluene by stirring. The bisimine ligand, CH₂ (Ph₂ P═NSiMe₃)₂, (1.16 g, 2.08 mmol) was added as a solid to the solution which was then heated to reflux at 130° C. for 24 hours. The resultant pale yellow solution was concentrated to nearly 5 mL and mixed with 5 mL of hexane. Upon cooling overnight, a pale yellow crystalline solid was obtained which was isolated by filtration (Yield: 1.05 g, 70.5%). IR (Nujol mull): 1653 w, 1480 w, 1462 m, 1436 s, 1378 w, 1304 s, 1251 s, 1179 w, 1156 w, 1112 s, 1061 s, 1042 s, 1026 m, 999 w, 842 s, 785 m, 771 w, 753 w, 747 w, 737 w, 714 s, 695 s, 652 s, 631 m, 613 s, 571 m, 522 s. ¹ H NMR (C₆ D₆): δ 7.6 (m, phenyl), 6.98 (m, phenyl), 6.92 (m, phenyl), 6.90 (m, phenyl), 0.25 (s, 18 H, CH₃ Si methyl). ¹³ C {¹ H} NMR (C₆ D₆): δ 134.2 (m, 4 C, ipso phenyl), 131.5 (t, ² J_(PC) =6.0 Hz, 8 C, ortho phenyl), 131.2 (s, 4 C, para phenyl), 128.5 (t, ³ J_(PC) =6.2 Hz, 8 C, meta phenyl), 101.7 (t, ¹ J_(PC) ═ 146 Hz, 1 C, PCP carbene), 2.6 (s, 6 C, CH₃ Si). ¹³ C {¹ H, ³¹ P} NMR (C₆ D₆): δ 134.2 (s, 4 C, ipso phenyl), 131.5 (s, 8 C, ortho phenyl), 131.2 (s, 4 C, para phenyl), 128.5 (s, 8 C, meta phenyl), 101.7 (s, 1 C, PCP carbene), 2.6 (s, 6 C, CH₃ Si). ³¹ P{¹ H} NMR (C₆ D₆): δ 15.7 (2 P). Analysis calculated for C₃₁ H₃₈ Cl₂ N₂ P₂ Si₂ Zr: C, 51.79; H, 5.33; N, 3.90. Found: C, 51.41; H, 5.78; N, 3.80.

Preparation of [ZrCl₂ {C(Ph₂ P═NSiMe₃)₂ }](Zr-3D) Method B

To a suspension of ZrCl₄ (THF)₂ (0.13 g, 0.35 mmol) in diethyl ether (5 ml) the dilithium salt Li₂ C(Ph₂ P═NSiMe₃)₂ 3 (0.20 g, 0.35 mmol) was added with stirring at room temperature. The mixture was stirred at room temperature for 2 days. Diethyl ether was removed and the resultant solid product was extracted with 5 mL of toluene and filtered to remove LiCl. The toluene solution was then concentrated to half the initial volume and the solution cooled to -15° C. for 2 days whereupon colorless crystals of {ZrCl₂ {C(Ph₂ P═NSiMe₃)₂ } precipitated (Yield: 0.16 g, 63.5%). All spectroscopic and analytical data indicated that the product was identical with the compound identified as {ZrCl₂ {C(Ph₂ P═NSiMe₃)₂ } as described above.

Preparation of [Zr{C(Ph₂ P═NSimMe₃)₂ }(CH₂ C₆ H₅)₂ ](Zr-6D)

[Zr(CH₂ C₆ H₅)₄ ] (1.0 g, 2.19 mmol) {literature preparation: Zucchini, U.; Albizzati, E.; Giannini, U.; J. Organomet. Chem. 1971, 26, 357-372.} was added to 15 mL of toluene and stirred at room temperature. To the pale yellow brown suspension was added solid bisimine ligand, CH₂ (Ph₂ P═NSiMe₃)₂ (1.226 g, 2.19 mmol) at room temperature. The reaction mixture was stirred at room temperature for 2 days during which time a pale brown microcrystalline solid precipitated. The product was isolated by filtration, washed with few mL of hexane and dried (Yield: 1.34 g, 73.5%). IR (Nujol mull): 1900-1650 w, 1591 m, 1488 m, 1481 m, 1466 m, 1436 m, 1378 m, 1334 w, 1283 s, 1260 s, 1249 s, 1216 m, 1204 m, 1173 m, 1151 w, 1110 s, 1016 b.s, 971 m, 880 w, 834 b.s, 793 w, 776 s, 764 m, 743 s, 734 m, 720 s, 693 s, 656 s, 620 m, 614 m, 562 s. ¹ H NMR (C₆ D₆): δ 7.34 (m, phenyl), 7.26 (m, phenyl), 7.24 (m, phenyl), 7.02 (m, phenyl), 6.93 (m, phenyl), 2.62 (s, 4H, CH₂ Ph methylene), 0.09 (s, 18 H, CH₃ Si methyl). ¹³ C {¹ H} (C₆ D₆): δ 147.7 (s, 2 C, ipso benzyl), 135.9 (m, 4 C, ipso phenyl), 131.6 (t, ² J_(PC) =6.0 Hz, 8 C, ortho phenyl), 130.5 (s, 4 C, ortho benzyl), 128.9 (s, 4 C, meta benzyl), 128.2 (t, ³ J_(PC) =6.5 Hz, 8 C, meta phenyl), 126.8 (s, 4 C, para phenyl), 121.2 (s, 2 C, para benzyl), 84.7 (t, ¹ J_(PC) =164 Hz, 1 C, PCP carbene), 68.8 (s, 2 C, CH₂ Ph methylene), 3.6 (s, 6 C, CH₃ Si). ¹³ C {¹ H, ³¹ P} NMR (C₆ D₆): δ 147.7 (s, 2 C, ipso benzyl), 135.9 (s, 4 C, ipso phenyl), 131.6 (s, 8 C, ortho phenyl), 130.5 (s, 4 C, ortho benzyl), 128.9 (s, 4 C, meta benzyl), 128.2 (s, 8 C, meta phenyl), 126.8 (s, 4 C, para phenyl), 121.2 (s, 2 C, para benzyl), 84.7 (s, 1 C, PCP carbene), 68.8 (s, 2 C, CH₂ Ph methylene), 3.6 (s, 6 C, CH₃ Si). ³¹ P{¹ H} NMR (C₆ D₆): δ 12.4 (2 P). Analysis calculated for C₄₅ H₅₂ N₂ P₂ Si₂ Zr: C, 65.10; H, 6.31; N, 3.37. Found: C, 65.65; H, 6.03; N, 3.31.

Preparation of [{(Me₃ SiN═PCy₂)₂ CH}Li(OEt₂)]

Colorless crystalline bis(dicyclohexylphosphoranotrimethylsilylimino)methane H₂ C{CY₂ P═NSiMe₃ }₂ (0.2 g, 0.34 mmol) was dissolved in 5 mL of toluene. To this solution MeLi was added (1.4 M solution in diethyl ether, 0.49 mL, 0.69 mmol) with stirring. The reaction mixture was stirred at room temperature for 3 days. Concentration of the mother solution to nearly half the original volume and leaving the flask at -15° C. for 48 hours yielded colorless crystals. (Yield: 0.145 g, 63.8%). IR (Nujol mull): 1269 m, 1242 s, 1223 s, 1211 s, 1197 s, 1167 s, 1151 s, 1113 m, 1071 w, 1007 m, 987 s, 893 m, 875 m, 850 s, 822 s, 777 m, 752 s, 730 w, 666 m, 641 w, 601 m, 562 s. ¹ H NMR (C₆ D₆): δ 3.39 (q, CH₂, Et₂ O), 2.05-1.24 (m, cyclohexyl), 1.09 (t, CH₃, Et₂ O), 0.03 (s, CH₃ Si), -0.02 (s, CH, P-CH-P). ¹³ C{¹ H} NMR (C₆ D₆): δ 65.2 (s, CH₂, Et₂ O), 41.2 (d, ¹ J_(PC) =63.0 Hz, ipso cyclohexyl), 27.5 (m, ortho & para cyclohexyl), 27.0 (s, meta cyclohexyl), 15.1(s, CH₃, Et₂ O), 5.3 (t, ¹ J_(PC) =128.6 Hz, CH, P-CH-P) 5.08 (s, CH₃ Si). ³¹ P{¹ H} NMR (C₆ D₆): δ 36.7 (2 P). Analysis calculated for C₃₅ H₇₃ LiN₂ OP₂ Si₂ : C, 63.43; H, 11.10; N, 4.23. Found: C, 63.19; H, 10.97 N, 4.30.

Preparation of [ZnMe{HC(Ph₂ P═NSiMe₃)₂ }](AK-17)

To a toluene (5 mL) solution of H₂ C(Ph₂ P═NSiMe₃)₂ (0.20 g, 0.36 mmol) ZnMe₂ (1.0 M solution in heptane, 0.36 mL, 0.36 mmol) was added with stirring at room temperature. Immediate evolution of a gas was observed. The reaction mixture was stirred at room temperature for one day. Concentration of the solution to half of the original volume and allowing this solution to stand at -15° C. for three days yielded colorless crystals. The product was filtered and dried in vacuum. Yield (0.145 g, 63.5). IR data (Nujol Mull): 1589 w, 1482 m, 1436 s, 1311 w, 1259 s, 1244 s, 1160 s, 1111 s, 1069 m, 1000 m, 927 s, 834 s, 803 s, 745 s, 729 s, 711 s, 695 s, 651 s, 615 m, 593 s, 547 s, 516 s. ¹ H NMR (C₆ D₆): δ 7.65 (m, phenyl), 7.00 (m, phenyl), 1.92(t, 1 H,² JHP=4.5 Hz), 0.17 (s, 3H, Me-Zn), 0.11 (s, 18 H. CH₃ Si methyl). ¹³ C{¹ H} NMR (C₆ D₆): 138.0 (m, ipso phenyl), 131.7 (t, ² J_(PC) =4.8 Hz, ortho phenyl), 130.3 (s, para phenyl), 128.1 (m, meta phenyl), 28.4 (t, P-CH-P, ¹ J_(PC) =120.6 Hz), 3.6 (t, CH₃ Si, ³ J_(PC) =1.8 Hz), -9.3 (s, Zn-Me). ³¹ P{¹ H} NMR (C₆ D₆): δ 26.2 (2 P). Analysis calculated for C₃₂ H₄₂ N₂ P₂ Si₂ Zn: C, 60.22; H, 6.63; N, 4.39. Found: C, 59.99; H, 6.62; N, 4.37.

Preparation of [ZnMe{HC(Cy₂ P═NSiMe₃)₂ }]

To a toluene (5 mL) solution of H₂ C(Cy₂ P═NSiMe₃)₂ (0.20 g, 0.34 mmol), ZnMe₂ (1.0 M solution in heptane, 0.34 mL, 0.34 mmol) was added with stirring at room temperature. Immediate evolution of gas was observed. The reaction mixture was stirred at room temperature for one day. Concentration of the solution to half of the original volume and allowing this solution to stand at -15° C. for few days gave colorless crystals. The product was filtered and dried in vacuum. Yield (0.15 g, 66.0%). IR data (Nujol Mull): 1450 s, 1324 w, 1246 s, 1217 s, 1204 s, 1168 m, 1139 s, 1096 s, 1043 m, 1028 w, 1004 m, 978 s, 914 w, 894 m, 887 m, 830 s, , 783 m, 768 m, 756 s, 734 m, 724 w, 676 m, 652 m, 615 m, 598 m, 553 s, 527 m. ¹ H NMR (C₆ D₆): δ 2.20-1.10(m, Cy), 1.03 (t, 1H, ² J_(HP) =0.7 Hz), 0.40 (s, 18 H, CH₃ Si methyl), -0.04 (s, 3H, Me-Zn). ¹³ C {¹ H} NMR (C₆ D₆): 40.7 (dd, ipso Cy), 27.5-26.7 (m, Cy), 6.8 (t, P-CH-P, ¹ J_(PC) =123.4 Hz), 4.77 (t, CH₃ Si, ³ J_(PC) =1.4 Hz), -7.52 (s, Me-Zn). ³¹ P{¹ H} NMR (C₆ D₆): δ 45.5 (2 P). Analysis calculated for C₃₂ H₆₆ N₂ P₂ Si₂ Zn: C, 58.02; H, 10.04; N, 4.23. Found: C, 57.99; H, 9.99; N, 4.18.

Preparation of [ZrCl₂ {HC(Ph₂ P═NSiMe₃)₂ }(OAd)]

The zirconium dichloride carbene complex, [ZrCl₂ {C(Ph₂ P═NSiMe₃)₂ }] (0.120 g, 0.17 mmol) was dissolved in 5 mL of toluene. To this colorless solution was added solid adamantanol (0.025 g, 0.17 mmol). With stirring a pale yellow solution was obtained. After 30 minutes, the solution was concentrated to nearly half of the original volume and mixed with few mL of hexane. Upon cooling overnight, a micro-crystalline solid was deposited which was isolated by filtration (Yield: 0.096 g, 66.0%). ¹ H NMR (toluene-d₈, 25° C.): δ 7.95 (b, phenyl), 7.09 (b, phenyl), 6.83 (b, phenyl), 6.63 (b, phenyl), 2.28 (t, ² J_(PH) =2.7 Hz, 1H, methine P-C-P), 2.17 (b. s, 6H, methylene Ad), 2.02 (b.s, 3H, methine Ad), 1.53 (b. dd, 6H, methylene Ad), 0.53 (s, 18H, methyl CH₃ Si). ³¹ P NMR (toluene-d₈, 25° C.): δ 20.1 (b.s, 2P).

Preparation of [ZrCl₂ {(C(O)(NAd))C(Ph₂ P═NSiMe₃)₂ }] (KB-103)

Solid adamantyl isocyanate (AdNCO) (0.049 g, 0.28 mmol) was added to a stirred, colorless solution of [ZrCl₂ {C(Ph₂ P═NSiMe₃)₂)}] (0.2 g, 0.28 mmol) in 10 mL of toluene. A white precipitate formed immediately. The resultant suspension was heated at 120° C. for few minutes to dissolve the precipitate. On cooling to room temperature, colorless crystals of the product precipitated which were separated by filtration (Yield: 0.185 g, 74.2%). ¹ H NMR (C₆ D₆): δ 8.23 (b. q, phenyl), 7.42 (b. q, phenyl), 7.12 (m, phenyl (toluene)), 7.06 (m, phenyl (toluene)), 7.01 (m, phenyl (toluene)), 6.64 (b. t, phenyl), 6.52 (b. t, phenyl), 2.12 (b. s, 6H, CH₂ -Ad methylene), 2.10 (s, CH₃ toluene), 1.88 (b. s, 3H, CH-Ad methine), 1.62 (b. d, ² J_(HH) =12.0 Hz, 3H, CH₂ -Ad methylene), 1.42 (d, ² J_(HH) =12.0 Hz, 3H, CH₂ -Ad methylene), 0.55 (s, 18 H, CH₃ Si methyl). ¹³ C {¹ H} NMR (C₆ D₆): δ 159.8 (t, 1C, ² J_(PC) =6.9 Hz, quaternary C═O), 137.9 (s, 2C, ipso phenyl (toluene)), 134.3 (t, ² J_(PC) =5.5 Hz, 8 C, ortho phenyl), 132.7 (s, 4 C, para phenyl), 131.98 (t, ³ J_(PC) =5.4 Hz, 8 C, meta phenyl), 131.6 (s, 4 C, ortho phenyl (toluene)), 130.1 (m, 4C, ipso phenyl), 129.3 (s, 4C, meta phenyl (toluene)), 125.6 (s, 2 C, para phenyl (toluene)), 57.6 (s, 1C, Ad quaternary carbon), 39.5 (s, 3C, CH₂ -Ad methylene), 36.9 (s, 3C, CH₂ -Ad methylene), 30.1 (s, 3C, CH-Ad methine), 24.7 (t, ¹ J_(PC) =98.0 Hz, 1 C, quaternary PCP carbon), 21.4 (s, CH₃ (toluene)), 4.6 (s, 6 C, CH₃ Si). ³¹ P{¹ H NMR (C₆ D₆): δ 24.6 (2 P).

Preparation of [HfCl₂ {(C(O)(NAd))C(Ph₂ P═NSiMe₃)₂ }]

Solid adamantyl isocyanate (0.044 g, 0.25 mmol) was added to a stirred colorless solution of [HfCl₂ {C(Ph₂ P═NSiMe₃)₂ }] (0.2 g, 0.25 mmol) in 10 mL of toluene. The reaction mixture was stirred at room temperature for an hour and left to stand at room temperature for two days. During that period colorless crystals formed which were subsequently isolated by filtration (0.17 g). The remaining mother liquor was concentrated to about 4 mL, layered with hexane and left to stand at -15° C. In two days second fraction of colorless crystals were obtained which were separated by filtration (0.064 g). The total yield was 0.234 g, 0.20 mmol, 80.8%. IR (Nujol mull): 1634 s, 1590 w, 1457 s, 1438 s, 1377 m, 1308 w, 1266 m, 1255 s, 1234 s, 1186 w, 1115 s, 1054 s, 1008 s, 924 w, 841 s, 773 s, 749 s, 727 s, 711 s, 695 m, 675 w, 659 m, 647 w, 616 m, 529 s, . ¹ H NMR (C₆ D₆): δ 8.24 (b. q, phenyl), 7.43 (b. q, phenyl), 7.08 (m, phenyl (toluene)), 7.04 (m, phenyl (toluene)), 7.01 (m, phenyl (toluene)), 6.65 (b. t, phenyl), 6.52 (b. t, phenyl), 2.12 (b. s, 6H, CH₂ -Ad methylene), 2.10 (s, 6H, CH₃ toluene), 1.90 (b. s, 3H, CH-Ad methine), 1.62 (b. d, ² J_(HH) =11.7 Hz, 3H, CH₂ -Ad methylene), 1.43 (b. d, ² J_(HH) =11.7 Hz, 3H, CH₂ -Ad methylene), 0.54 (s, 18 H, CH₃ Si methyl). ¹³ C {¹ H} NMR (C₆ D₆): δ 159.7 (t, 1C, ² J_(PC) =6.4 Hz, quaternary C═O), 137.8 (s, 2C, ipso phenyl (toluene)), 134.3 (t, ² J_(PC) =5.5 Hz, 8 C, ortho phenyl), 132.6 (s, 4 C, para phenyl), 131.9 (t, ³ J_(PC) =5.2 Hz, 8 C, meta phenyl), 131.6 (s, 4 C, ortho phenyl (toluene)), 130.3 (m, 4C, ipso phenyl), 129.3 (s, 4C, meta phenyl (toluene)), 125.6 (s, 2 C, para phenyl (toluene)), 56.6 (s, 1 C, Ad quaternary carbon), 39.6 (s, 3C, CH₂ -Ad methylene), 36.9 (s, 3C, CH₂ -Ad methylene), 30.2 (s, 3C, CH-Ad methine), 25.2 (t, ¹ J_(PC) =97.1 Hz, 1 C, quatemary PCP carbon), 21.4 (s, 2 C, CH₃ (toluene)), 4.7 (s, 6 C, CH₃ Si). ³¹ P{¹ H} NMR (C₆ D₆): δ 24.8 (2 P). Analysis calculated for C₄₅.5 H₅₇ Cl₂ HfN₃ OP₂ Si₂ : C, 53.08; H, 5.58; N, 4.08. Found: C, 53.58; H, 5.73; N, 3.94. (The crystal becomes opaque when it was taken out of solvent and slowly loses the lattice solvent molecules. So the analysis was calculated based on the formula [HfCl₂ {(C(O)(NAd))-C(Ph₂ P═NSiMe₃)₂ }]0.5C₆ H₅ CH₃ 9).

Preparation of [Sm{C(Ph₂ P═NSiMe₃)₂ -(NCy₂)(THF)]

To a toluene (4 mL) solution of [Sm(NCy₂)₃ (THF)] (0.205 g, 0.268 mmol), H₂ C(Ph₂ P═NSiMe₃)₂ (0.15 g, 0.268 mmol) was added with stirring at room temperature. The reaction mixture was stirred at room temperature for a day and then refluxed for 30 minutes. Cooling the solution to room temperature and allowing the flask to stand for two days gave bright yellow crystals which were isolated by filtration. The crystals were dried under vacuum. Yield: 0.14 g, 54.4%. IR data (Nujol Mull): 1435 s, 1341 w, 1243 s, 1177 w, 1146 m, 1107 s, 1086 s, 1065 s, 1026 s, 948 m, 917 w, 886 m, 834 s, 763 s, 749 s, 729 m, 713 s, 699 s, 678 w, 659 m, 648 m, 608 s, 548 s, 521 s, 511 s, 480 s, . ³¹ P{¹ H} NMR (C₆ D₆): δ 43.3 (br.s). Analysis calculated for C₄₇ H₆₈ N₃ OP₂ Si₂ Sm: C, 58.83; H, 7.14; N, 4.38. Found: C, 59.39; H, 7.25; N, 4.40.

Polymerization Conditions and Results

In the examples, the pressures given are gauge pressures. The following abbreviations and terms are used:

Branching: reported as the number of methyl groups per 1000 methylene groups in the polymer. It is determined by FT-IR.

Polydispersity: weight average molecular weight (Mw) divided by number average molecular weight (Mn).

DSC: differential scanning calorimetry.

GPC: gel permeation chromatography.

MeOH: methanol.

PMAO-IP: a type of polymethylaluminoxane.

Anhydrous toluene was purchased from Aldrich and purified over molecular sieves prior to use. PMAO-IP was purchased from Akzo-Nobel and contained 13.5 wt. % of Al. B(C₆ F₅)₃ was purchased from Boulder Scientific Inc. and used without further purification. [CPh₃ ][B(C₆ F₅)₄ ] was purchased from Asahi Glass Inc.; lot #: 980224.

Polymer molecular weights and molecular weight distributions were measured by GPC (Waters 150-C) at 140° C. in 1,2,4-trichlorobenzene calibrated using polyethylene standards.

FT-IR was conducted on a Nicolet Model 750 Magna IR spectrometer.

DSC was conducted on a DSC 220 C from Seiko Instruments. The heating rate is 10° C./minute from 0 to 200° C.

Part A: Solution Phase Polymerization

All the solution polymerization experiments described below were conducted using an Autoclave Engineers Zipperclave reactor (500 mL). All the chemicals (solvent, catalyst and cocatalyst) were fed into the reactor batchwise except ethylene which was fed on demand. No product was removed during the polymerization reaction. As are known to those skilled in the art, all the feed streams were purified prior to feeding into the reactor by contact with various absorption media to remove catalysts killing impurities such as water, oxygen, sulfur and polar materials. All components were stored and manipulated under an atmosphere of purified argon or nitrogen. The reactor uses a programmable logical control (PLC) system with Wonderware 5.1 s, oftware for the process control. Ethylene polymerizations were performed in the reactor equipped with an air driven stirrer and an automatic temperature control system.

The catalyst was dissolved in toluene. Polymerization temperature is as indicated in the table below. The polymerization reaction time is typically 10 minutes. The reaction was terminated by adding 5 mL of methanol to the reactor and the polymer was recovered by evaporation of the solvent. The polymerization activities were calculated based on the ethylene consumption.

Examples 1-18 were conducted on a solution semi-batch reactor (SBR).

SBR Experimental Conditions with MAO Activation

    ______________________________________                                         Cyclohexane       216 mL                                                         Catalyst Concentration 200 μmol/L                                           PMAO-IP Al/Zr = 300 (mol/mol)                                                  Reaction Temperature 160° C.                                            Reactor Pressure 140 psig total                                                Stirring Speed 2000 rpm                                                      ______________________________________                                    

SBR Experirimental Conditions with Trinitylborate Activation

    ______________________________________                                         Cyclohexane      216 mL                                                          Catalyst Concentration 200 μmol/L                                           PMAO-IP 1 mmol/L as impurity scavenger                                         [CPh.sub.3 ][B(C.sub.6 F.sub.5).sub.4 ] 210 μmol/L                          Reaction Temperature 160° C.                                            Reactor Pressure 140 psig total                                                Stirring Speed 2000 rpm                                                      ______________________________________                                    

SBR Results

    __________________________________________________________________________     SBR Results                                                                                      Activity                                                          gPE/                                                                        Examples Catalyst  mmol cat* Polymer Properties                              (1-18)                                                                              Code Cocatalyst                                                                             hr   Mw*10.sup.-3                                                                        Mn*10.sup.-3                                                                        PD                                            __________________________________________________________________________      1.sup.a                                                                            Zr-3D                                                                               PMAO-IP 14.2 52.5 0.45 116.7                                            2.sup.a Zr-3C PMAO-IP 22.7 67.3 0.25 269.2                                     3.sup.b Zr-3C [CPh.sub.3 ][B(C.sub.6 F.sub.5).sub.4 ] 70.6 643.6 139.1                                       4.63                                             4.sup.c Zr-6D [CPh.sub.3 ][B(C.sub.6 F.sub.5).sub.4 ] 11.6 153.9 38.1                                        4.04                                             5.sup.d Zr-6D [CPh.sub.3 ][B(C.sub.6 F.sub.5).sub.4 ] 42.7 535.1 78.7                                        6.8                                              6.sup.c Zr-6D B(C.sub.6 F.sub.5)3 9.12 316.2 20.1 15.73                        7.sup.e Zr-6D [CPh.sub.3 ][B(C.sub.6 F.sub.5).sub.4 ] 14.4 199.2 3.45                                        57.7                                             8.sup.c Zr-3C- [CPh.sub.3 ][B(C.sub.6 F.sub.5).sub.4 ] 56.8 449.1                                            127.1 3.53                                       Me2                                                                            9.sup.f Zr-6D [CPh.sub.3 ][B(C.sub.6 F.sub.5).sub.4 ] 10.5 94.8 2.08                                         45.6                                            10.sup.f Zr-3C- [CPh.sub.3 ][B(C.sub.6 F.sub.5).sub.4 ] 8.22                    Me2                                                                           11.sup.b Ak-61 [CPh.sub.3 ][B(C.sub.6 F.sub.5).sub.4 ] 67.7                    12.sup.f AK-61 [CPh.sub.3 ][B(C.sub.6 F.sub.5).sub.4 ] 68.7                    13.sup.b KB-103 [CPh.sub.3 ][B(C.sub.6 F.sub.5).sub.4 ] 498.7                  14.sup.a KB-103 PMAO-IP 129.0                                                  15.sup.c AK-17 [CPh.sub.3 ][B(C.sub.6 F.sub.5).sub.4 ] 89.78                   16.sup.g AK-17 [CPh.sub.3 ][B(C.sub.6 F.sub.5).sub.4 ]                         17.sup.h DuPont PMAO-IP 49.46 15 1.1 14.4                                       Catalyst                                                                      18.sup.a Cp.sub.2 ZrCl.sub.2 PMAO-IP 1339.9 7.8 2.2 4.6                      __________________________________________________________________________      .sup.a SBR standard MAO screening conditions.                                  .sup.b Insitu alkylation: PMAOIP (Al/M = 20) premixed with catalyst, the       mixture and tritylborate solution were injected into the reactor               simultaneously.                                                                .sup.c SBR standard trityl borate screening conditions.                        .sup.d Premix catalyst and cocatalyst.                                         .sup.e Zr(Bz).sub.4 as scavenger at 1.2 mmol/L.                                .sup.f Copolymerization with 20 mL of 1octene. Polymerization activities       were calculated based on polymer weight. 20.7 Br/1000 C detected by NMR        for copolymer produced in run 12.                                              .sup.g It is a slurry polymerization conducted in toluene.                     .sup.h DuPont Ni diimine catalyst was synthesized according to a publishe      procedure (L. K. Johnson, C. M. Killiam, M. Brookhart, J. Am. Chem. Soc.,      117, 6414, 1995).                                                        

Part B: Gas Phase Polymerization Catalyst Preparation and Polymerization Testing Using a Semi-Batch, Gas Phase Reactor

The catalyst preparation methods described below employ typical techniques for the syntheses and handling of air-sensitive materials. Standard Schlenk and drybox techniques were used in the preparation of ligands, metal complexes, support substrates and supported catalyst systems. Solvents were purchased as anhydrous materials and further treated to remove oxygen and polar impurities by contact with a combination of activated alumina, molecular sieves and copper oxide on silica/alumina. Where appropriate, elemental compositions of the supported catalysts were measured by Neutron Activation analysis and a reported accuracy of ±1% (weight basis).

The supported catalysts were prepared by initially supporting MAO on a silica support, followed by deposition of the catalyst component.

All the polymerization experiments described below were conducted using a semi-batch, gas phase polymerization reactor of total internal volume of 2.2 L. Reaction gas mixtures, including ethylene were measured to the reactor on a continuous basis using a calibrated thermal mass flow meter, following passage through purification media as described above. A pre-determined mass of the catalyst sample was added to the reactor under the flow of the inlet gas with no pre-contact of the catalyst with any reagent, such as a catalyst activator. The catalyst was activated in situ (in the polymerization reactor) at the reaction temperature in the presence of the monomer, using a metal alkyl complex which has been previously added to the reactor to remove adventitious impurities. Purified and rigorously anhydrous sodium chloride was used as a catalyst dispersing agent.

The internal reactor temperature is monitored by a thermocouple in the polymerization medium and can be controlled at the required set point to +/-1.0° C. The duration of the polymerization experiment was one hour. Following the completion of the polymerization experiment, the polymer was separated from the sodium chloride and the yield determined. The following table illustrates bench scale gas phase reaction conditions.

Bench Scale Reactor Operating Conditions for Gas Phase Polymerizations

    ______________________________________                                         Solvent        5-10 mL hexane added with catalyst                                Operating Mode Gas Phase                                                       Aluminum alkyl 25-30 wt. % triisobutyl aluminum                                Al:Ti 250:1                                                                    Hydrogen None                                                                  Comonomer None                                                                 Reaction Pressure 200 psig                                                     Reaction Temperature 90° C.                                             Reaction Time 60 minutes                                                     ______________________________________                                    

Examples 19-22 are examples of the gas phase polymerization. The next table illustrates data concerning the Al/transition metal ratios of the supported catalyst, polymer yield and polymer properties.

Polymerization Results

    ______________________________________                                                         Amount of  Yield PE                                                                              gPE/g gPE/g                                    Examples Catalyst Catalyst (mg) (g) Metal Catalyst                           ______________________________________                                         19     AK-17    50         0        0   0                                        20 AK-61 54 1.8 6962 33                                                        21 Zr-3D 50 0   0 0                                                            22 KB-103 52 0.4 1607 8                                                      ______________________________________                                          .sup.1 Homopolymerization                                                      .sup.2 PE = Polyethylene                                                 

Part C: Slurry Phase Polymerization Catalyst Preparation and Polymerization Testing Using a Semi-Batch, Gas Phase Reactor

Part C1: High Temperature and Pressure Slurry Polymerization

The supported catalyst described in Part B was also used for the slurry polymerization tests.

All the polymerization experiments described below were conducted using a semi-batch reactor of total internal volume of 2.2 L. Reaction gas mixtures, including ethylene were measured to the reactor on a continuous basis using a calibrated thermal mass flow meter, following passage through purification media as described above. A pre-determined mass of the catalyst sample as added to the reactor under the flow of the inlet gas with no pre-contact of the catalyst with any reagent, such as a catalyst activator. The catalyst was activated in situ (in the polymerization reactor) at the reaction temperature in the presence of the monomer, using a metal alkyl complex and solvent which have been previously added to the reactor to remove adventitious impurities.

The internal reactor temperature is monitored by a thermocouple in the polymerization medium and can be controlled at the required set point to +/-1.0° C. The duration of the polymerization experiment was one hour. Following the completion of the polymerization experiment, the slurry was transferred from the reactor to a bowl, and the solvent was left to evaporate. The following table illustrates bench scale slurry phase reaction conditions.

Bench Scale Reactor Operating Conditions for Slurry Polymerizations

    ______________________________________                                         Solvent         750 mL hexane                                                    Operating Mode Slurry Phase                                                    Aluminum alkyl 25-30 wt. % triisobutyl aluminum                                Al:Ti 250:1                                                                    Hydrogen None                                                                  Comonomer None                                                                 Reaction Pressure 200 psig                                                     Reaction Temperature 90° C.                                             Reaction Time 60 minutes                                                     ______________________________________                                    

Examples 23-24 are high pressure and temperature slurry polymerization examples. The next table illustrates data concerning the Al/transition metal ratios of the supported catalyst; polymer yield and polymer properties.

Polymerization Results

    ______________________________________                                                         Amount of  Yield PE                                                                              gPE/g gPE/g                                    Examples Catalyst Catalyst (mg) (g) Metal Catalyst                           ______________________________________                                         23     AK-61    122        3.5    5992  29                                       24 Zr-3D 137 0.6  915  4                                                     ______________________________________                                          .sup.1 Homopolymerization                                                      .sup.2 PE = Polyethylene                                                 

Part C2: Low Temperature and Pressure Slurry Polymerization

Low pressure and temperature slurry polymerization experiments were conducted on a catalyst screening unit (CSU) where polymerization occurs in a cyclohexane reaction media, ethylene is fed to the reactor on demand and is monitored by a mass flow meter. On the CSU, reaction temperatures are monitored and controlled by thermocouples and one RTD. Reactor temperature control is maintained by a HAAKE circulating water bath which has external thermostatic control via the thermocouple at the reactor core. Reactor temperature is maintained by the water from the bath entering the jacket-like coolant chamber surrounding the reactor. Reaction pressures are indicated by mechanical pressure gauges and monitored manually.

The CSU shares the purified ethylene and cyclohexane feeds with the solution semi-batch reactor (SBR). Ultra-High-Purity argon from PRAXAIR which is purified further by 13× and OXICLEAR on a separate gas purification unit is used for reactor system purging and solvent sparging. The polymerization products are quantitatively recovered for mass determination, and polymerization activities are then calculated based upon mass of product, millimoles of catalyst injected and reaction time.

Examples 25-32 were conducted on a catalyst screening unit (CSU).

CSU Standard MAO Screening Conditions

    ______________________________________                                         Cyclohexane      300 mL                                                          Catalyst Concentration 50 μmol/L (Zr)                                       Catalyst Mole Ratio Al/Zr = 500/1                                               Polymethylaluminoxane (PMAO-IP)                                               Reaction Temperature Setpoint 35° C.                                    Reactor Pressure Setpoint 10 psig total                                        Stirring Speed ˜2250 +/- 300 rpm Initially                             ______________________________________                                    

CSU Standard Tritylborate Screening Conditions

    ______________________________________                                         Cyclohexane     300 mL                                                           Catalyst Concentration 50 μmol/L (M)                                        Catalyst Mole Ratio Al/B/M = 20/1.05/1                                          Modified Methylaluminoxane (MMAO-                                              7)/trityl borate                                                              Reaction Temperature Setpoint 35° C.                                    Reactor Pressure Setpoint 10 psig total                                        Stirring Speed ˜2250 +/- 300 rpm Initially                             ______________________________________                                    

CSU Polymerization Results

    ______________________________________                                                Catalyst                 Activity                                         Examples Code Cocatalyst gPE/mmol cat*hr                                     ______________________________________                                         25     Cp.sub.2 ZrCl.sub.2                                                                        PMAO-IP      2692                                             26 Zr-3D PMAO-IP 1                                                             27 Zr-3C PMAO-IP 0                                                             28 Zr-6D PMAO-IP 13                                                            29 Zr-3C-Me.sub.2 MMAO- 29                                                       7/[CPh.sub.3 ][B(C.sub.6 F.sub.5).sub.4 ]                                    30 KB-103 PMAO-IP 0                                                            31 AK-17 MMAO- 4                                                                 7/[CPh.sub.3 ][B(C.sub.6 F.sub.5).sub.4 ]                                    32 AK-61 PMAO-IP 116                                                         ______________________________________                                     

What is claimed is:
 1. A process for the polymerization of one or more C₂₋₁₂ alpha olefins in the presence of a complex selected from the group consisting of:(a) a complex of formula I: ##STR11## wherein M is a metal atom selected from the group consisting of a transition metal, a post transition metal and a lanthanide; R¹, R², R³ and R⁴ are independently selected from the group consisting of a hydrogen atom, a saturated or unsaturated straight chained, branched or cyclic hydrocarbyl radical which is unsubstituted or substituted by one or more substituents selected from the group consisting of a halogen atom and a C₁₋₆ alkyl radical; R⁷ and R⁸ are independently selected from the group consisting of a halogen atom, an alkyl, an amide --NR¹ R², an alkoxide or aryl oxide group --OR¹, and an --OSi(R¹)₃ group wherein R¹ and R² are defined above, a saturated or unsaturated straight chained, branched or cyclic hydrocarbyl radical which are unsubstituted or substituted by a halogen atom or a C₁₋₆ alkyl radical, and a Lewis base which may contain a donor heteroatom, and each R⁵ is independently selected from the group consisting of radicals selected from the group consisting of saturated and unsaturated straight chained, branched and cyclic hydrocarbyl radicals, C₆₋₁₂ cyclic aliphatic or aromatic radical; radicals of the formula Si(R⁶)₃ wherein each R⁶ is independently selected from the group consisting of saturated or unsaturated straight chained, branched or cyclic hydrocarbyl radicals, and radicals of the formula III: ##STR12## wherein R⁹, R¹⁰, R¹¹ and R¹² are independently selected from the group consisting of a hydrogen atom, a fluorine atom, a NO₂ radical, a C₁₋₆ alkyl radical, and a C₈₋₁₂ aryl radical and E is an endocyclic nitrogen atom or a C--CN group; (b) a complex of formula II: ##STR13## wherein M, R¹, R², R³, R⁴, R⁵, R⁷ and R⁸ are as defined above and R¹⁴ is selected from the group consisting of a hydrogen atom and a C₁₋₂₀ hydrocarbyl radical which may contain a terminal functional group; and optionally R¹⁴ taken together with M may form a constrained ring; and c) a complex of formula V: ##STR14## wherein M, R¹, R², R³, R⁴ and R⁵ are as defined above; and an activator at a temperature from 20 to 250° C. and at a pressure from 15 to 15,000 psi.
 2. The process according to claim 1, wherein the activator is selected from the group consisting of:(i) aluminoxane compounds R₂₀ ₂ AlO(R²⁰ AlO)_(m) AlR²⁰ ₂ wherein each R²⁰ is independently selected from the group consisting of C₁₋₂₀ hydrocarbyl radical and m is from 5 to 30 to provide a molar ratio of aluminum to M from 20:1 to 1000:1; (ii) anions of the formula [B(R¹⁸)₄ ]⁻ wherein each R¹⁸ is independently selected from the group consisting of phenyl radicals which are unsubstituted or substituted by up to 5 s, ubstituents selected from the group consisting of a fluorine atom, a C₁₋₄ alkyl or alkoxy radical which is unsubstituted or substituted by a fluorine atom and a silyl radical of the formula --Si(R¹⁹)₃ ; wherein each R¹⁹ is independently selected from the group consisting of a hydrogen atom and a C₁₋₄ alkyl radical; and an activator of the formula [B(R¹⁸)₃ ] wherein R¹⁸ is as defined above and to provide a molar ratio of M to boron from 1:1 to 1:3; and (iii) a mixture of activators (i) and (ii) and an aluminum compound selected from the group consisting of aluminum alkyls of the formula AlR_(3-n) X_(n) in which R is independently selected from the group consisting of a C₁₋₈ alkyl radical, X is a halogen atom and n is 0, 1, 2 or 3 to provide a ratio M to aluminum to boron from 1:1:1 to 1:100:5.
 3. The process according to claim 2, wherein M is selected from the group consisting of Y, Ti, Zr, Hf, V, Cr, Fe, Co, Ni, Pd, Zn and Sm.
 4. The process according to claim 3, wherein the complex R¹, R², R³ and R⁴ are selected from the group consisting of C₁₋₁₀ s, traight chained, branched or cyclic alkyl radicals which are unsubstituted or substituted by up to three substituents selected from the group consisting of a chlorine atom, a fluorine atom and a C₁₋₄ alkyl radical and C₅₋₁₄ aromatic radicals which are unsubstituted or further substituted by up to n-1, wherein n is the number of carbon atoms in the aromatic radical substituents selected from the group consisting of a fluorine atom, a chlorine atom and a C₁₋₆ alkyl radical or an amido radical which is unsubstituted or substituted by up to two C₁₋₆ alkyl radicals.
 5. The process according to claim 4, wherein the complex R¹, R², R³ and R⁴ are selected from the group consisting of a hydrogen atom, a fluorine atom, a chlorine atom, a methyl radical, an ethyl radical, a propyl radical, a butyl radical, a tertiary butyl radical and a phenyl radical.
 6. The process according to claim 4, wherein the complex is of formula I or formula II.
 7. The process according to claim 6, wherein the complex R⁷ and R⁸ are selected from the group consisting of a chlorine atom, a fluorine atom, a C₁₋₁₀ s, traight chained, branched or cyclic alkyl radicals which are unsubstituted or substituted by up to three substituents selected from the group consisting of a chlorine atom, a fluorine atom and a C₁₋₄ alkyl radical; an amide of the formula --NR¹ R² where in R¹ and R² are C₁₋₄ alkyl radicals; C₅₋₁₄ aromatic radicals which are unsubstituted or further substituted by up to n-1, wherein n is the number of carbon atoms in the aromatic radical substituents selected from the group consisting of a fluorine atom, a chlorine atom and a C₁₋₆ alkyl radical or an amido radical which is unsubstituted or substituted by up to two C₁₋₆ alkyl radicals; C₁₋₆ alkyl ethers, C₄₋₈ cyclic ethers; C₁₋₆ tertiary amines; cyclic C₄₋₈ nitrogen containing compounds; and tertiary C₁₋₁₀ phosphines.
 8. The process according to claim 7, wherein the complex at least one of R⁷ and R⁸ is a C₅₋₁₃ ligand containing a 5-membered carbon ring having delocalized bonding within the ring and bound to the metal atom through covalent η⁵ bonds.
 9. The process according to claim 8, wherein the complex at least one of R⁷ and R⁸ is selected from the group consisting of cyclopentadienyl, indenyl and fluorenyl which are unsubstituted or up to fully substituted by a member selected from the group consisting of a chlorine atom, a fluorine atom, and an amido radical which is unsubstituted or substituted by up to two C₁₋₄ alkyl radicals.
 10. The process according to claim 9, wherein the complex one or more R⁵ s, ubstituents are selected from the group consisting of C₁₋₆ alkyl radicals and C₆₋₁₂ cyclic aliphatic or aromatic radicals.
 11. The process according to claim 10, wherein R⁵ is selected from the group consisting of methyl, ethyl, butyl, phenyl and adamantyl radicals.
 12. The process according to claim 9, wherein one or more R⁵ substituents is a radical of the formula III: ##STR15## wherein R⁹, R¹⁰, R¹¹ and R¹² are independently selected from the group consisting of a hydrogen atom, a fluorine atom, a NO₂ radical, a C₁₋₆ alkyl radical, and a C₈₋₁₂ aryl radical and E is an endocyclic nitrogen atom or a C--CN group.
 13. The process according to claim 12, wherein E is an endocyclic nitrogen atom.
 14. The process according to claim 12, wherein E is a C--CN group.
 15. The process according to claim 9, wherein one or more R⁵ substituents is selected from the group consisting of radicals of the formula Si(R⁶)₃ wherein each R⁶ is independently selected from the group consisting of C₁₋₁₀ s, aturated or unsaturated straight chained, branched or cyclic hydrocarbyl radicals.
 16. The process according to claim 15, wherein R⁶ is selected from the group consisting of methyl, ethyl, propyl and butyl radicals.
 17. The process according to claim 11, wherein the complex is of formula I.
 18. The process according to claim 17, wherein the temperature is from 120 to 250° C., the pressure is from 100 to 4,500 psig, the activator is an aluminoxane of the formula (R²⁰)₂ AlO(R²⁰ AlO)_(m) Al(R²⁰)₂ in which each R²⁰ is selected from the group consisting of C₁₋₄ alkyl radicals and m is from 5 to
 30. 19. The process according to claim 17, wherein the temperature is from 20 to 120° C., the pressure is from 15 to 4,500 psig, the activator is an aluminoxane of the formula (R²⁰)₂ AlO(R²⁰ AlO)_(m) Al(R²⁰)₂ in which each R²⁰ is selected from the group consisting of C₁₋₄ alkyl radicals and m is from 5 to
 30. 20. The process according to claim 17, wherein the temperature is from 120 to 250° C., the pressure is from 100 to 4,500 psig and the activator is an ionic activator selected from the group consisting of N,N-dimethylaniliniumtetrakispentafluorophenyl borate, triphenylmethylium tetrakispentafluorophenyl borate and trispentafluorophenyl boron.
 21. The process according to claim 17, wherein the temperature is from 20 to 120° C., the pressure is from 15 to 4,500 psig and the activator is an ionic activator selected from the group consisting of N,N-dimethylaniliniumtetrakispentafluorophenyl borate, triphenylmethylium tetrakispentafluorophenyl borate and trispentafluorophenyl boron.
 22. The process according to claim 11, wherein the complex is of formula II and R¹⁴ is selected from the group consisting of a hydrogen atom and C₁₋₄ alkyl radicals.
 23. The process according to claim 22, wherein the temperature is from 120 to 250° C., the pressure is from 100 to 4,500 psig, the activator is an aluminoxane of the formula (R²⁰)₂ AlO(R²⁰ AlO)_(m) Al(R²⁰)₂ in which each R²⁰ is selected from the group consisting of C₁₋₄ alkyl radicals and m is from 5 to
 30. 24. The process according to claim 22, wherein the temperature is from 20 to 120° C., the pressure is from 15 to 4,500 psig, the activator is an aluminoxane of the formula (R²⁰)₂ AlO(R²⁰ AlO)_(m) Al(R²⁰)₂ in which each R²⁰ is selected from the group consisting of C₁₋₄ alkyl radicals and m is from 5 to
 30. 25. The process according to claim 26, wherein the temperature is from 120 to 250° C., the pressure is from 100 to 4,500 psig and the activator is an ionic activator selected from the group consisting of N,N-dimethylaniliniumtetrakispentafluorophenyl borate, triphenylmethylium tetrakispentafluorophenyl borate and trispentafluorophenyl boron.
 26. The process according to claim 22, wherein the temperature is from 20 to 120° C., the pressure is from 15 to 4,500 psig and the activator is an ionic activator selected from the group consisting of N,N-dimethylaniliniumtetrakispentafluorophenyl borate, triphenylmethylium tetrakispentafluorophenyl borate and trispentafluorophenyl boron.
 27. The process according to claim 13, wherein the complex is of formula I.
 28. The process according to claim 27, wherein the temperature is from 120 to 250° C., the pressure is from 100 to 4,500 psig, the activator is an aluminoxane of the formula (R²⁰)₂ AlO(R²⁰ AlO)_(m) Al(R²⁰)₂ in which each R²⁰ is selected from the group consisting of C₁₋₄ alkyl radicals and m is from 5 to
 30. 29. The process according to claim 27, wherein the temperature is from 20 to 120° C., the pressure is from 15 to 4,500 psig, the activator is an aluminoxane of the formula (R²⁰)₂ AlO(R²⁰ AlO)_(m) Al(R²⁰)₂ in which each R²⁰ is selected from the group consisting of C₁₋₄ alkyl radicals and m is from 5 to
 30. 30. The process according to claim 27, wherein the temperature is from 120 to 250° C., the pressure is from 100 to 4,500 psig and the activator is an ionic activator selected from the group consisting of N,N-dimethylaniliniumtetrakispentafluorophenyl borate, triphenylmethylium tetrakispentafluorophenyl borate and trispentafluorophenyl boron.
 31. The process according to claim 27, wherein the temperature is from 20 to 120° C., the pressure is from 15 to 4,500 psig and the activator is an ionic activator selected from the group consisting of N,N-dimethylaniliniumtetrakispentafluorophenyl borate, triphenylmethylium tetrakispentafluorophenyl borate and trispentafluorophenyl boron.
 32. The process according to claim 13, wherein the complex is of formula II and R¹⁴ is selected from the group consisting of a hydrogen atom and C₁₋₄ alkyl radicals.
 33. The process according to claim 32, wherein the temperature is from 120 to 250° C., the pressure is from 100 to 4,500 psig, the activator is an aluminoxane of the formula (R²⁰)₂ AlO(R²⁰ AlO)_(m) Al(R²⁰)₂ in which each R²⁰ is selected from the group consisting of C₁₋₄ alkyl radicals and m is from 5 to
 30. 34. The process according to claim 32, wherein the temperature is from 20 to 120° C., the pressure is from 15 to 4,500 psig, the activator is an aluminoxane of the formula (R²⁰)₂ AlO(R²⁰ AlO)_(m) Al(R²⁰)₂ in which each R²⁰ is selected from the group consisting of C₁₋₄ alkyl radicals and m is from 5 to
 30. 35. The process according to claim 32, wherein the temperature is from 120 to 250° C., the pressure is from 100 to 4,500 psig and the activator is an ionic activator selected from the group consisting of N,N-dimethylaniliniumtetrakispentatluorophenyl borate, triphenylmethylium tetrakispentafluorophenyl borate and trispentafluorophenyl boron.
 36. The process according to claim 32, wherein the temperature is from 20 to 120° C., the pressure is from 15 to 4,500 psig and the activator is an ionic activator selected from the group consisting of N,N-dimethylaniliniumtetrakispentafluorophenyl borate, triphenylmethylium tetrakispentafluorophenyl borate and trispentafluorophenyl boron.
 37. The process according to claim 14, wherein the complex is of formula I.
 38. The process according to claim 37, wherein the temperature is from 120 to 250° C., the pressure is from 100 to 4,500 psig, the activator is an aluminoxane of the formula (R²⁰)₂ AlO(R²⁰ AlO)_(m) Al(R²⁰)₂ in which each R²⁰ is selected from the group consisting of C₁₋₄ alkyl radicals and m is from 5 to
 30. 39. The process according to claim 37, wherein the temperature is from 20 to 120° C., the pressure is from 15 to 4,500 psig, the activator is an aluminoxane of the formula (R²⁰)₂ AlO(R²⁰ AlO)_(m) Al(R²⁰)₂ in which each R²⁰ is selected from the group consisting of C₁₋₄ alkyl radicals and m is from 5 to
 30. 40. The process according to claim 37, wherein the temperature is from 120 to 250° C., the pressure is from 100 to 4,500 psig and the activator is an ionic activator selected from the group consisting of N,N-dimethylaniliniumtetrakispentafluorophenyl borate, triphenylmethylium tetrakispentafluorophenyl borate and trispentafluorophenyl boron.
 41. The process according to claim 37, wherein the temperature is from 20 to 120° C., the pressure is from 15 to 4,500 psig and the activator is an ionic activator selected from the group consisting of N,N-dimethylaniliniumtetrakispentafluorophenyl borate, triphenylmethylium tetrakispentafluorophenyl borate and trispentafluorophenyl boron.
 42. The process according to claim 38, wherein said one or more R⁵ substituents are a 4-cyanotetrafluorophenyl radical.
 43. The process according to claim 39, wherein said one or more R⁵ substituents are a 4-cyanotetrafluorophenyl radical.
 44. The process according to claim 40, wherein said one or more R⁵ substituents are a 4-cyanotetrafluorophenyl radical.
 45. The process according to claim 41, wherein said one or more R⁵ substituents are a 4-cyanotetrafluorophenyl radical.
 46. The process according to claim 14, wherein the complex is of formula II and R¹⁴ is selected from the group consisting of a hydrogen atom and C₁₋₄ alkyl radicals.
 47. The process according to claim 46, wherein the temperature is from 120 to 250° C., the pressure is from 100 to 4,500 psig, the activator is an aluminoxane of the formula (R²⁰)₂ AlO(R²⁰ AlO)_(m) Al(R²⁰)₂ in which each R²⁰ is selected from the group consisting of C₁₋₄ alkyl radicals and m is from 5 to
 30. 48. The process according to claim 46, wherein the temperature is from 20 to 120° C., the pressure is from 15 to 4,500 psig, the activator is an aluminoxane of the formula (R²⁰)₂ AlO(R²⁰ AlO)_(m) Al(R²⁰)₂ in which each R²⁰ is selected from the group consisting of C₁₋₄ alkyl radicals and m is from 5 to
 30. 49. The process according to claim 46, wherein the temperature is from 120 to 250° C., the pressure is from 100 to 4,500 psig and the activator is an ionic activator selected from the group consisting of N,N-dimethylaniliniumtetrakispentafluorophenyl borate, triphenylmethylium tetrakispentafluorophenyl borate and trispentafluorophenyl boron.
 50. The process according to claim 46, wherein the temperature is from 20 to 120° C., the pressure is from 15 to 4,500 psig and the activator is an ionic activator selected from the group consisting of N,N-dimethylaniliniumtetrakispentafluorophenyl borate, triphenylmethylium tetrakispentafluorophenyl borate and trispentafluorophenyl boron.
 51. The process according to claim 47, wherein said one or more R⁵ substituents are a 4-cyanotetrafluorophenyl radical.
 52. The process according to claim 47, wherein said one or more R⁵ substituents are a 4-cyanotetrafluorophenyl radical.
 53. The process according to claim 47, wherein said one or more R⁵ substituents are a 4-cyanotetrafluorophenyl radical.
 54. The process according to claim 47, wherein said one or more R⁵ substituents are a 4-cyanotetrafluorophenyl radical.
 55. The process according to claim 16, wherein the complex is of formula I.
 56. The process according to claim 55, wherein the temperature is from 120 to 250° C., the pressure is from 100 to 4,500 psig, the activator is an aluminoxane of the formula (R²⁰)₂ AlO(R²⁰ AlO)_(m) Al(R²⁰)₂ in which each R²⁰ is selected from the group consisting of C₁₋₄ alkyl radicals and m is from 5 to
 30. 57. The process according to claim 55, wherein the temperature is from 20 to 120° C., the pressure is from 15 to 4,500 psig, the activator is an aluminoxane of the formula (R²⁰)₂ AlO(R²⁰ AlO)_(m) Al(R²⁰)₂ in which each R²⁰ is selected from the group consisting of C₁₋₄ alkyl radicals and m is from 5 to
 30. 58. The process according to claim 55, wherein the temperature is from 120 to 250° C., the pressure is from 100 to 4,500 psig and the activator is an ionic activator selected from the group consisting of N,N-dimethylaniliniumtetrakispentafluorophenyl borate, triphenylmethylium tetrakispentafluorophenyl borate and trispentafluorophenyl boron.
 59. The process according to claim 55, wherein the temperature is from 20 to 120° C., the pressure is from 15 to 4,500 psig and the activator is an ionic activator selected from the group consisting of N,N-dimethylaniliniumtetrakispentafluorophenyl borate, triphenylmethylium tetrakispentafluorophenyl borate and trispentafluorophenyl boron.
 60. The process according to claim 16, wherein the complex is of formula II and R¹⁴ is selected from the group consisting of a hydrogen atom and C₁₋₄ alkyl radicals.
 61. The process according to claim 60, wherein the temperature is from 120 to 250° C., the pressure is from 100 to 4,500 psig, the activator is an aluminoxane of the formula (R²⁰)₂ AlO(R²⁰ AlO)_(m) Al(R²⁰)₂ in which each R²⁰ is selected from the group consisting of C₁₋₄ alkyl radicals and m is from 5 to
 30. 62. The process according to claim 60, wherein the temperature is from 20 to 120° C., the pressure is from 15 to 4,500 psig, the activator is an aluminoxane of the formula (R²⁰)₂ AlO(R²⁰ AlO)_(m) Al(R²⁰)₂ in which each R²⁰ is selected from the group consisting of C₁₋₄ alkyl radicals and m is from 5 to
 30. 63. The process according to claim 60, wherein the temperature is from 120 to 250° C., the pressure is from 100 to 4,500 psig and the activator is an ionic activator selected from the group consisting of N,N-dimethylaniliniumtetrakispentafluorophenyl borate, triphenylmethylium tetrakispentafluorophenyl borate and trispentafluorophenyl boron.
 64. The process according to claim 60, wherein the temperature is from 20 to 120° C., the pressure is from 15 to 4,500 psig and the activator is an ionic activator selected from the group consisting of N,N-dimethylaniliniumtetrakispentafluorophenyl borate, triphenylmethylium tetrakispentafluorophenyl borate and trispentafluorophenyl boron.
 65. The process according to claim 5, wherein the complex is of formula V.
 66. The process according to claim 65, wherein the complex one or more R⁶ substituents are selected from the group consisting of C₁₋₆ alkyl radicals and C₆₋₁₂ cyclic aliphatic or aromatic radicals.
 67. The process according to claim 66, wherein R⁵ is selected from the group consisting of methyl, ethyl, butyl, phenyl and adamantyl radicals.
 68. The process according to claim 66, wherein one or more R⁵ substituents is a radical of the formula III: ##STR16## wherein R⁹, R¹⁰, R¹¹ and R¹² are independently selected from the group consisting of a hydrogen atom, a fluorine atom, a NO₂ radical, a C₁₋₆ alkyl radical, and a C₈₋₁₂ aryl radical and E is an endocyclic nitrogen atom or a C--CN group.
 69. The process according to claim 68, wherein E is an endocyclic nitrogen atom.
 70. The process according to claim 68, wherein E is a C--CN group.
 71. The process according to claim 66, wherein one or more R⁵ substituents is selected from the group consisting of radicals of the formula Si(R⁶)₃ wherein each R⁶ is independently selected from the group consisting of C₁₋₁₀ s, aturated or unsaturated straight chained, branched or cyclic hydrocarbyl radicals.
 72. The process according to claim 71, wherein R⁶ is selected from the group consisting of methyl, ethyl, propyl and butyl radicals.
 73. The process according to claim 67, wherein the temperature is from 120 to 250° C., the pressure is from 100 to 4,500 psig, the activator is an aluminoxane of the formula (R²⁰)₂ AlO(R²⁰ AlO)_(m) Al(R²⁰)₂ in which each R²⁰ is selected from the group consisting of C₁₋₄ alkyl radicals and m is from 5 to
 30. 74. The process according to claim 67, wherein the temperature is from 20 to 120° C., the pressure is from 15 to 4,500 psig, the activator is an aluminoxane of the formula (R²⁰)₂ AlO(R²⁰ AlO)_(m) Al(R²⁰)₂ in which each R²⁰ is selected from the group consisting of C₁₋₄ alkyl radicals and m is from 5 to
 30. 75. The process according to claim 67, wherein the temperature is from 120 to 250° C., the pressure is from 100 to 4,500 psig and the activator is an ionic activator selected from the group consisting of N,N-dimethylaniliniumtetrakispentafluorophenyl borate, triphenylmethylium tetrakispentafluorophenyl borate and trispentafluorophenyl boron.
 76. The process according to claim 67, wherein the temperature is from 20 to 120° C., the pressure is from 15 to 4,500 psig and the activator is an ionic activator selected from the group consisting of N,N-dimethylaniliniumtetrakispentafluorophenyl borate, triphenylmethylium tetrakispentafluorophenyl borate and trispentafluorophenyl boron.
 77. The process according to claim 69, wherein the temperature is from 120 to 250° C., the pressure is from 100 to 4,500 psig, the activator is an aluminoxane of the formula (R²⁰)₂ AlO(R²⁰ AlO)_(m) Al(R²⁰)₂ in which each R²⁰ is selected from the group consisting of C₁₋₄ alkyl radicals and m is from 5 to
 30. 78. The process according to claim 69, wherein the temperature is from 20 to 120° C., the pressure is from 15 to 4,500 psig, the activator is an aluminoxane of the formula (R²⁰)₂ AlO(R²⁰ AlO)_(m) Al(R²⁰)₂ in which each R²⁰ is selected from the group consisting of C₁₋₄ alkyl radicals and m is from 5 to
 30. 79. The process according to claim 69, wherein the temperature is from 120 to 250° C., the pressure is from 100 to 4,500 psig and the activator is an ionic activator selected from the group consisting of N,N-dimethylaniliniumtetrakispentafluorophenyl borate, triphenylmethylium tetrakispentafluorophenyl borate and trispentafluorophenyl boron.
 80. The process according to claim 69, wherein the temperature is from 20 to 120° C., the pressure is from 15 to 4,500 psig and the activator is an ionic activator selected from the group consisting of N,N-dimethylaniliniumtetrakispentafluorophenyl borate, triphenylmethylium tetrakispentafluorophenyl borate and trispentafluorophenyl boron.
 81. The process according to claim 70, wherein the temperature is from 120 to 250° C., the pressure is from 100 to 4,500 psig, the activator is an aluminoxane of the formula (R²⁰)₂ AlO(R²⁰ AlO)_(m) Al(R²⁰)₂ in which each R²⁰ is selected from the group consisting of C₁₋₄ alkyl radicals and m is from 5 to
 30. 82. The process according to claim 70, wherein the temperature is from 20 to 120° C., the pressure is from 15 to 4,500 psig, the activator is an aluminoxane of the formula (R²⁰)₂ AlO(R²⁰ AlO)_(m) Al(R²⁰)₂ in which each R²⁰ is selected from the group consisting of C₁₋₄ alkyl radicals and m is from 5 to
 30. 83. The process according to claim 70, wherein the temperature is from 120 to 250° C., the pressure is from 100 to 4,500 psig and the activator is an ionic activator selected from the group consisting of N,N-dimethylaniliniumtetrakispentafluorophenyl borate, triphenylmethylium tetrakispentafluorophenyl borate and trispentafluorophenyl boron.
 84. The process according to claim 70, wherein the temperature is from 20 to 120° C., the pressure is from 15 to 4,500 psig and the activator is an ionic activator selected from the group consisting of N,N-dimethylaniliniumtetrakispentafluorophenyl borate, triphenylmethylium tetrakispentafluorophenyl borate and trispentafluorophenyl boron.
 85. The process according to claim 81, wherein said one or more R⁵ substituents are a 4-cyanotetrafluorophenyl radical.
 86. The process according to claim 82, wherein said one or more R⁵ substituents are a 4-cyanotetrafluorophenyl radical.
 87. The process according to claim 83, wherein said one or more R⁵ substituents are a 4-cyanotetrafluorophenyl radical.
 88. The process according to claim 84, wherein said one or more R⁵ substituents are a 4-cyanotetrafluorophenyl radical.
 89. The process according to claim 72, wherein the temperature is from 120 to 250° C., the pressure is from 100 to 4,500 psig, the activator is an aluminoxane of the formula (R²⁰)₂ AlO(R²⁰ AlO)_(m) Al(R²⁰)₂ in which each R²⁰ is selected from the group consisting of C₁₋₄ alkyl radicals and m is from 5 to
 30. 90. The process according to claim 72, wherein the temperature is from 20 to 120° C., the pressure is from 15 to 4,500 psig, the activator is an aluminoxane of the formula (R²⁰)₂ AlO(R²⁰ AlO)_(m) Al(R²⁰)₂ in which each R²⁰ is selected from the group consisting of C₁₋₄ alkyl radicals and m is from 5 to
 30. 91. The process according to claim 72, wherein the temperature is from 120 to 250° C., the pressure is from 100 to 4,500 psig and the activator is an ionic activator selected from the group consisting of N,N-dimethylaniliniumtetrakispentafluorophenyl borate, triphenylmethylium tetrakispentafluorophenyl borate and trispentafluorophenyl boron.
 92. The process according to claim 72, wherein the temperature is from 20 to 120° C., the pressure is from 15 to 4,500 psig and the activator is an ionic activator selected from the group consisting of N,N-dimethylaniliniumtetrakispentafluorophenyl borate, triphenylmethylium tetrakispentafluorophenyl borate and trispentafluorophenyl boron. 